CN112352007B - Method for producing a mixture of polymers - Google Patents
Method for producing a mixture of polymers Download PDFInfo
- Publication number
- CN112352007B CN112352007B CN201980041453.XA CN201980041453A CN112352007B CN 112352007 B CN112352007 B CN 112352007B CN 201980041453 A CN201980041453 A CN 201980041453A CN 112352007 B CN112352007 B CN 112352007B
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- China
- Prior art keywords
- ch2f
- cof
- formula
- compound
- polymer mixture
- Prior art date
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- 229920000642 polymer Polymers 0.000 title claims abstract description 64
- 239000000203 mixture Substances 0.000 title claims description 75
- 238000004519 manufacturing process Methods 0.000 title abstract description 10
- 150000001875 compounds Chemical class 0.000 claims abstract description 161
- 238000000034 method Methods 0.000 claims abstract description 84
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 14
- 229920000570 polyether Polymers 0.000 claims abstract description 13
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 12
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 7
- 229920002959 polymer blend Polymers 0.000 claims description 174
- VUWZPRWSIVNGKG-UHFFFAOYSA-N fluoromethane Chemical compound F[CH2] VUWZPRWSIVNGKG-UHFFFAOYSA-N 0.000 claims description 83
- XJHCXCQVJFPJIK-UHFFFAOYSA-M caesium fluoride Chemical group [F-].[Cs+] XJHCXCQVJFPJIK-UHFFFAOYSA-M 0.000 claims description 50
- 229910052731 fluorine Inorganic materials 0.000 claims description 49
- 239000011737 fluorine Substances 0.000 claims description 28
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 26
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 21
- 125000002947 alkylene group Chemical group 0.000 claims description 19
- 238000003682 fluorination reaction Methods 0.000 claims description 19
- 229910052799 carbon Inorganic materials 0.000 claims description 18
- 125000004432 carbon atom Chemical group C* 0.000 claims description 18
- 125000000217 alkyl group Chemical group 0.000 claims description 16
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 15
- 238000006114 decarboxylation reaction Methods 0.000 claims description 14
- FPGGTKZVZWFYPV-UHFFFAOYSA-M tetrabutylammonium fluoride Chemical compound [F-].CCCC[N+](CCCC)(CCCC)CCCC FPGGTKZVZWFYPV-UHFFFAOYSA-M 0.000 claims description 12
- 125000001153 fluoro group Chemical group F* 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 10
- 229910052739 hydrogen Inorganic materials 0.000 claims description 10
- REYHXKZHIMGNSE-UHFFFAOYSA-M silver monofluoride Chemical group [F-].[Ag+] REYHXKZHIMGNSE-UHFFFAOYSA-M 0.000 claims description 8
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 claims description 7
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 claims description 7
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 claims description 7
- -1 perfluoro compound Chemical class 0.000 claims description 7
- 150000001265 acyl fluorides Chemical group 0.000 claims description 6
- AOGYCOYQMAVAFD-UHFFFAOYSA-N chlorocarbonic acid Chemical group OC(Cl)=O AOGYCOYQMAVAFD-UHFFFAOYSA-N 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 6
- AHLATJUETSFVIM-UHFFFAOYSA-M rubidium fluoride Chemical group [F-].[Rb+] AHLATJUETSFVIM-UHFFFAOYSA-M 0.000 claims description 6
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 238000006116 polymerization reaction Methods 0.000 claims description 5
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 claims description 5
- 150000001336 alkenes Chemical class 0.000 claims description 4
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 claims description 4
- 125000001183 hydrocarbyl group Chemical group 0.000 claims description 4
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 4
- 125000004430 oxygen atom Chemical group O* 0.000 claims description 4
- 239000011698 potassium fluoride Chemical group 0.000 claims description 4
- 229920002313 fluoropolymer Polymers 0.000 claims description 3
- ZVJOQYFQSQJDDX-UHFFFAOYSA-N 1,1,2,3,3,4,4,4-octafluorobut-1-ene Chemical compound FC(F)=C(F)C(F)(F)C(F)(F)F ZVJOQYFQSQJDDX-UHFFFAOYSA-N 0.000 claims description 2
- PBWHQPOHADDEFU-UHFFFAOYSA-N 1,1,2,3,3,4,4,5,5,5-decafluoropent-1-ene Chemical compound FC(F)=C(F)C(F)(F)C(F)(F)C(F)(F)F PBWHQPOHADDEFU-UHFFFAOYSA-N 0.000 claims description 2
- RMHCWMIZBMGHKV-UHFFFAOYSA-N 1,1,2,3,3,4,4,5,5,6,6,6-dodecafluorohex-1-ene Chemical compound FC(F)=C(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F RMHCWMIZBMGHKV-UHFFFAOYSA-N 0.000 claims description 2
- CDAVUOSPHHTNBU-UHFFFAOYSA-N 1,1,2,3,3,4,4,5,5,6,6,7,7,7-tetradecafluorohept-1-ene Chemical compound FC(F)=C(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F CDAVUOSPHHTNBU-UHFFFAOYSA-N 0.000 claims description 2
- YCBPKOZNGFQMPB-UHFFFAOYSA-N 1,1,2,3,3,4,4,5,5,6,6,7,7,8,8,8-hexadecafluorooct-1-ene Chemical compound FC(F)=C(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F YCBPKOZNGFQMPB-UHFFFAOYSA-N 0.000 claims description 2
- LGPPATCNSOSOQH-UHFFFAOYSA-N 1,1,2,3,4,4-hexafluorobuta-1,3-diene Chemical compound FC(F)=C(F)C(F)=C(F)F LGPPATCNSOSOQH-UHFFFAOYSA-N 0.000 claims description 2
- BLTXWCKMNMYXEA-UHFFFAOYSA-N 1,1,2-trifluoro-2-(trifluoromethoxy)ethene Chemical compound FC(F)=C(F)OC(F)(F)F BLTXWCKMNMYXEA-UHFFFAOYSA-N 0.000 claims description 2
- WUMVZXWBOFOYAW-UHFFFAOYSA-N 1,2,3,3,4,4,4-heptafluoro-1-(1,2,3,3,4,4,4-heptafluorobut-1-enoxy)but-1-ene Chemical compound FC(F)(F)C(F)(F)C(F)=C(F)OC(F)=C(F)C(F)(F)C(F)(F)F WUMVZXWBOFOYAW-UHFFFAOYSA-N 0.000 claims description 2
- BZPCMSSQHRAJCC-UHFFFAOYSA-N 1,2,3,3,4,4,5,5,5-nonafluoro-1-(1,2,3,3,4,4,5,5,5-nonafluoropent-1-enoxy)pent-1-ene Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)=C(F)OC(F)=C(F)C(F)(F)C(F)(F)C(F)(F)F BZPCMSSQHRAJCC-UHFFFAOYSA-N 0.000 claims description 2
- ZFFLXJVVPHACEG-UHFFFAOYSA-N 1,2,3,3,4,4,5,5,6,6-decafluorocyclohexene Chemical compound FC1=C(F)C(F)(F)C(F)(F)C(F)(F)C1(F)F ZFFLXJVVPHACEG-UHFFFAOYSA-N 0.000 claims description 2
- YBMDPYAEZDJWNY-UHFFFAOYSA-N 1,2,3,3,4,4,5,5-octafluorocyclopentene Chemical compound FC1=C(F)C(F)(F)C(F)(F)C1(F)F YBMDPYAEZDJWNY-UHFFFAOYSA-N 0.000 claims description 2
- QVHWOZCZUNPZPW-UHFFFAOYSA-N 1,2,3,3,4,4-hexafluorocyclobutene Chemical compound FC1=C(F)C(F)(F)C1(F)F QVHWOZCZUNPZPW-UHFFFAOYSA-N 0.000 claims description 2
- IJTAKAGEJXIJPQ-UHFFFAOYSA-N 3-chloro-1,1,2,3,3-pentafluoroprop-1-ene Chemical compound FC(F)=C(F)C(F)(F)Cl IJTAKAGEJXIJPQ-UHFFFAOYSA-N 0.000 claims description 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims description 2
- QDGONURINHVBEW-UHFFFAOYSA-N dichlorodifluoroethylene Chemical group FC(F)=C(Cl)Cl QDGONURINHVBEW-UHFFFAOYSA-N 0.000 claims description 2
- NROKBHXJSPEDAR-UHFFFAOYSA-M potassium fluoride Chemical compound [F-].[K+] NROKBHXJSPEDAR-UHFFFAOYSA-M 0.000 claims description 2
- 229940096017 silver fluoride Drugs 0.000 claims description 2
- 229910004261 CaF 2 Chemical group 0.000 claims 2
- ABADUMLIAZCWJD-UHFFFAOYSA-N 1,3-dioxole Chemical class C1OC=CO1 ABADUMLIAZCWJD-UHFFFAOYSA-N 0.000 claims 1
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- 229930195733 hydrocarbon Natural products 0.000 claims 1
- 239000011521 glass Substances 0.000 abstract description 6
- 239000000654 additive Substances 0.000 abstract description 3
- 238000000576 coating method Methods 0.000 abstract description 3
- 239000004033 plastic Substances 0.000 abstract description 3
- 229920003023 plastic Polymers 0.000 abstract description 3
- 238000006243 chemical reaction Methods 0.000 description 36
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 25
- ZUHZGEOKBKGPSW-UHFFFAOYSA-N tetraglyme Chemical compound COCCOCCOCCOCCOC ZUHZGEOKBKGPSW-UHFFFAOYSA-N 0.000 description 18
- 230000007062 hydrolysis Effects 0.000 description 15
- 238000006460 hydrolysis reaction Methods 0.000 description 15
- 239000000047 product Substances 0.000 description 15
- 238000005160 1H NMR spectroscopy Methods 0.000 description 12
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 12
- 230000007935 neutral effect Effects 0.000 description 10
- 238000006068 polycondensation reaction Methods 0.000 description 10
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 9
- FZFAMSAMCHXGEF-UHFFFAOYSA-N chloro formate Chemical compound ClOC=O FZFAMSAMCHXGEF-UHFFFAOYSA-N 0.000 description 9
- 239000002904 solvent Substances 0.000 description 9
- 238000005481 NMR spectroscopy Methods 0.000 description 8
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 8
- 150000002148 esters Chemical class 0.000 description 8
- 239000000843 powder Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 6
- 238000004821 distillation Methods 0.000 description 6
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 6
- 125000001820 oxy group Chemical group [*:1]O[*:2] 0.000 description 6
- 239000010702 perfluoropolyether Substances 0.000 description 6
- 239000011541 reaction mixture Substances 0.000 description 6
- 230000009257 reactivity Effects 0.000 description 6
- IRHYACQPDDXBCB-UHFFFAOYSA-N 1,2,3,4-tetrachloro-1,1,2,3,4,4-hexafluorobutane Chemical compound FC(F)(Cl)C(F)(Cl)C(F)(Cl)C(F)(F)Cl IRHYACQPDDXBCB-UHFFFAOYSA-N 0.000 description 5
- KJOOJFLEZNWPIN-UHFFFAOYSA-N 2,2-difluoropropanedioyl difluoride Chemical compound FC(=O)C(F)(F)C(F)=O KJOOJFLEZNWPIN-UHFFFAOYSA-N 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 125000005843 halogen group Chemical group 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 125000003118 aryl group Chemical group 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 125000003709 fluoroalkyl group Chemical group 0.000 description 4
- 230000014509 gene expression Effects 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 239000012299 nitrogen atmosphere Substances 0.000 description 4
- JQMFQLVAJGZSQS-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-N-(2-oxo-3H-1,3-benzoxazol-6-yl)acetamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)CC(=O)NC1=CC2=C(NC(O2)=O)C=C1 JQMFQLVAJGZSQS-UHFFFAOYSA-N 0.000 description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- IUHFWCGCSVTMPG-UHFFFAOYSA-N [C].[C] Chemical group [C].[C] IUHFWCGCSVTMPG-UHFFFAOYSA-N 0.000 description 3
- 125000002252 acyl group Chemical group 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 125000004185 ester group Chemical group 0.000 description 3
- 238000005886 esterification reaction Methods 0.000 description 3
- 239000001307 helium Substances 0.000 description 3
- 229910052734 helium Inorganic materials 0.000 description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 3
- 238000002955 isolation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- FDGCJTUAVVJFMB-UHFFFAOYSA-N 2,2,3,3,4,4,5,5-octafluorohexanedioyl difluoride Chemical compound FC(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)=O FDGCJTUAVVJFMB-UHFFFAOYSA-N 0.000 description 2
- KNURRSZDMIXZLO-UHFFFAOYSA-N 2,2,3,3-tetrafluorobutanedioyl difluoride Chemical compound FC(=O)C(F)(F)C(F)(F)C(F)=O KNURRSZDMIXZLO-UHFFFAOYSA-N 0.000 description 2
- PUAQLLVFLMYYJJ-UHFFFAOYSA-N 2-aminopropiophenone Chemical compound CC(N)C(=O)C1=CC=CC=C1 PUAQLLVFLMYYJJ-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 150000001335 aliphatic alkanes Chemical group 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- HFNQLYDPNAZRCH-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O.OC(O)=O HFNQLYDPNAZRCH-UHFFFAOYSA-N 0.000 description 2
- 238000003442 catalytic alkylation reaction Methods 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 125000001309 chloro group Chemical group Cl* 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- SBZXBUIDTXKZTM-UHFFFAOYSA-N diglyme Chemical compound COCCOCCOC SBZXBUIDTXKZTM-UHFFFAOYSA-N 0.000 description 2
- 238000004508 fractional distillation Methods 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- 125000001188 haloalkyl group Chemical group 0.000 description 2
- PGFXOWRDDHCDTE-UHFFFAOYSA-N hexafluoropropylene oxide Chemical compound FC(F)(F)C1(F)OC1(F)F PGFXOWRDDHCDTE-UHFFFAOYSA-N 0.000 description 2
- 150000002430 hydrocarbons Chemical group 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 238000006384 oligomerization reaction Methods 0.000 description 2
- 125000000962 organic group Chemical group 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000003880 polar aprotic solvent Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- YFNKIDBQEZZDLK-UHFFFAOYSA-N triglyme Chemical compound COCCOCCOCCOC YFNKIDBQEZZDLK-UHFFFAOYSA-N 0.000 description 2
- 125000006659 (C1-C20) hydrocarbyl group Chemical group 0.000 description 1
- DZKXDEWNLDOXQH-UHFFFAOYSA-N 1,3,5,2,4,6-triazatriphosphinine Chemical group N1=PN=PN=P1 DZKXDEWNLDOXQH-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical group F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- 239000002841 Lewis acid Substances 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 150000001266 acyl halides Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 125000000732 arylene group Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001721 carbon Chemical group 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical group 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001212 derivatisation Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000007350 electrophilic reaction Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 150000002431 hydrogen Chemical group 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 150000007517 lewis acids Chemical class 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 229910001512 metal fluoride Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- QLOAVXSYZAJECW-UHFFFAOYSA-N methane;molecular fluorine Chemical compound C.FF QLOAVXSYZAJECW-UHFFFAOYSA-N 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000012038 nucleophile Substances 0.000 description 1
- 230000000269 nucleophilic effect Effects 0.000 description 1
- 238000007344 nucleophilic reaction Methods 0.000 description 1
- 238000010534 nucleophilic substitution reaction Methods 0.000 description 1
- 150000002921 oxetanes Chemical class 0.000 description 1
- 125000005702 oxyalkylene group Chemical group 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007348 radical reaction Methods 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000001356 surgical procedure Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/32—Polymers modified by chemical after-treatment
- C08G65/321—Polymers modified by chemical after-treatment with inorganic compounds
- C08G65/323—Polymers modified by chemical after-treatment with inorganic compounds containing halogens
- C08G65/3233—Molecular halogen
- C08G65/3236—Fluorine
-
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- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
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- C08G65/005—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from unsaturated compounds containing halogens
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- C08L71/00—Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
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Abstract
The present invention relates to a process for the synthesis of partially fluorinated and fully fluorinated polyether (PFPE) polymers, PFPE polymers obtained therefrom and the use of said PFPE polymers as intermediate compounds for the manufacture of additives for plastics and glass coatings.
Description
Cross Reference to Related Applications
The present application claims priority from european application No. 18168488.7 filed on 4.20.2018, the entire contents of which are incorporated herein by reference for all purposes.
Technical Field
The present invention relates to a process for the synthesis of partially fluorinated and fully fluorinated polyether (PFPE) polymers, PFPE polymers obtained therefrom and the use of said PFPE polymers as intermediate compounds for the manufacture of additives for plastics and glass coatings.
Background
Among fluorinated polymers, (per) fluoropolyether polymers (PFPE) are well known and of great interest for their chemical and physical properties, which makes them particularly interesting as lubricants.
The synthesis of several PFPE polymers has been disclosed in the art. The first synthesis of unspecified perfluorinated polyether mixtures was reported in 1953, when an oily product was obtained during the photo-oligomerization (photo-oligomerization) of hexafluoropropylene. Since then, a number of different perfluorinated polyethers have been synthesized and described in the literature. (ALLEN, geoffrey et al COMPREHENSIVE POLYMER SCIENCE-Second supplement [ comprehensive Polymer Science-second supplement ]. Edited by SIR ALLEN, geoffrey et al [ edited by SIR ALLEN, geoffrey et al ]. Elsevier Science [ Esculence ],1996.ISBN 0080427081. Pages 347-388 ].
For example, catalytic polymerization of perfluoroepoxides, such as notably hexafluoropropylene oxide (HFPO), first disclosed by DuPont (Du Pont) researchers, yields the product nameCommercially available products whose backbone comprises a polymer having the formula- [ CF (CF 3 )CF 2 O] y -a repeating unit. Then, monte Edison (Montelison) researchers have disclosed photochemical oxidation of perfluoro-olefins such as tetrafluoroethylene and hexafluoropropylene, which resulted in the trade name +.>Commercially available products whose backbone comprises a random distribution of the formula- [ (CF) 2 O) m (CF 2 CF(R)O) n ]-a repeating unit wherein R is-F or-CF 3 . Another synthesis involving ring-opening polymerization of partially fluorinated oxetanes followed by fluorination is disclosed by Daikin Company (Daikin Company) and yields the product name +.>Commercially available products whose backbone comprises a polymer having the formula- (CF) 2 CF 2 CF 2 O) p -a repeating unit.
The main difference between the (per) fluoropolyether polymers known in the art lies in the fact that:polymer and->The polymer is a homopolymer characterized by an ordered structure comprising only one type of repeating unit, i.e., - [ CF (CF) 3 )CF 2 O] y -and- (CF) 2 CF 2 CF 2 O) p -. Differently, +.>A polymer is a copolymer characterized by the presence of two or more (also defined as statistically distributed) repeating units of different formulae and randomly distributed along the backbone chain. This random distribution of repeating units is due to the manufacturing process based on photochemical oxidation of perfluoroolefins. However, a random distribution of repeating units may result in a polymer comprising a plurality of continuous repeating units having one carbon atom (i.e., having the formula-CF 2 The main chain chains of O-) which on the one hand increase the flexibility of the polymer main chain, but on the other hand constitute weaknesses in the polymer main chain, since they are more vulnerable to attack by metals and/or lewis acids.
Partially fluorinated compounds and methods for their preparation have been disclosed in the art.
For example, in US20040192974 (SOLVAY SOLEXIS s.p.a.), a process for obtaining hydrofluoroether compounds comprising (per) fluorooxyalkylene chains containing recurring units statistically distributed along the chain is disclosed.
In addition, WO 2010/057691 (sor visualex) discloses the synthesis of hydrofluoroalcohols having formula (I):
A-(R f ) a -CFX-O-R h -O-(CFX-(R f ) a* -CFX-O-R h -O) n H(I)
wherein R is h Is a divalent C1-C20 hydrocarbyl residue,
x is F or C1-C6- (per) fluoroalkyl,
R f is a (per) fluoro (poly) oxyalkylene (PFPE) chain or a (per) fluoroalkyl chain. According to a preferred embodiment, R f Is composed of one or more compounds of formula- (C) 3 F 6 O)-、-(CF 2 O)-、-(CF 2 CF 2 O)-、-(CF 2 CF 2 CF 2 O)-、-(CF 2 CF 2 CF 2 CF 2 O)-、-[CF(CF 3 )O]-PFPE chains of repeating units, thisThe repeating units are statistically (i.e., randomly) distributed along the chain.
However, none of the above documents discloses or suggests a partial or complete fluorination (perfluorinated) reaction of the hydrofluorocompounds obtained herein.
Synthesis of alpha-omega-dimethoxy fluoropolyethers is disclosed in AVATANEO, marco et al, synthesis of alfa-omega-dimethoxy fluoropolyethers: reaction mechanism and kinetics [ synthesis of alpha-omega-dimethoxy fluoropolyethers: reaction mechanism and kinetics ]Journal of Fluorine Chemistry journal of fluorine chemistry]2005, vol.126, pages 633-639 and GALIMBERTI, marco et al New catalytic alkylation of in situ generated perfluoro-alkoxy-anions and perfluoro-carbanions [ in situ generated perfluoro-alkoxy-anions and novel catalytic alkylation of perfluorocarbanions ]]Journal of Fluorine Chemistry journal of fluorine chemistry]2005, volume 126, pages 1578-1586. However, the synthesis disclosed in these articles starts from alkyl chloroformates and perfluoropolyether diacyl fluorides, the latter being obtained by photopolymerization. In other words, the perfluoropolyether comprises at one chain end a group of formula-C (O) F, but it also comprises a group of formula- (CF) randomly distributed within the backbone of the polymer 2 CF 2 O) -and- (CF) 2 O) -repeat units.
US2016137947 (glabrous schiff ltd (ASAHI GLASS COMPANY LIMITED)) discloses fluorinated polyether compounds according to the formula:
{X-O-[(CF 2 CF 2 O) a -(CF 2 CF 2 CF 2 CF 2 O) b ]} m -Y-{[(OCF 2 CF 2 ) c -(OCF 2 CF 2 CF 2 CF 2 ) d ]-O-Z} n
wherein the method comprises the steps of
m is from 1 to 10;
n is from 0 to 10;
x is a group having a hydroxyl group, a carboxyl group, an ester group or an aryl group;
y is an (m+n) -valent alkane group, an (m+n) -valent alkane group having an ether oxygen atom interposed between carbon-carbon atoms, (m+n) A fluoroalkyl group having a valence, a fluoroalkyl group having a valence of (m+n) having an ether oxygen atom interposed between carbon-carbon atoms, or a cyclotriphosphazene structure (P 3 N 3 ) The method comprises the steps of carrying out a first treatment on the surface of the And is also provided with
Z is a group having no hydroxyl group, carboxyl group, ester group or aryl group and having a haloalkyl group (provided that the halogen atom is a fluorine atom or a chlorine atom), or a haloalkyl group having an ether oxygen interposed between carbon-carbon atoms (provided that the halogen atom is a fluorine atom or a chlorine atom). In part- [ (CF) 2 CF 2 O) a -(CF 2 CF 2 CF 2 CF 2 O) b ]In the number "a" of units (CF 2 CF 2 O) and "b" number of units (CF 2 CF 2 CF 2 CF 2 O) is not limited, i.e. the order of connection of the units (CF 2 CF 2 O) and (CF) 2 CF 2 CF 2 CF 2 O) may be randomly positioned, alternately arranged, or at least one of a plurality of units (CF 2 CF 2 O) and units (CF) 2 CF 2 CF 2 CF 2 The blocks of O) may be linked. The structure of the formula is preferred-CF 2 CF 2 O(CF 2 CF 2 CF 2 CF 2 OCF 2 CF 2 O) e -
Wherein e is from 1 to 99.
Disclosure of Invention
The applicant faced the problem of preparing a perfluoropolyether polymer mixture having a predefined chemical structure, i.e. a perfluoropolyether polymer characterized by repeating units distributed in the polymer backbone, is non-random but a priori defined and in which the fraction of reactive groups (also called functional groups) that can be further functionalized or given a particular reactivity can be appropriately adjusted.
Similarly, there is an unmet need in the art for perfluoropolyether polymer mixtures having well-defined sequences of repeating units, and wherein the average functionality and/or relative concentration of reactive end chains can be achieved without burdensome purification/isolation processes.
Surprisingly, the applicant has found a process which can be conveniently applied on an industrial scale to mixtures of synthetic compounds having repeat units which are not randomly distributed in the main chain, while the nature of the end groups can be suitably adjusted.
Thus, in a first aspect, the invention relates to a process for the synthesis of a mixture [ polymer mixture (FH CH2F )]Method [ method (P) FH )]Each of the chain ends is attached to an opposite side of the backbone, wherein the first chain end [ end (Re 1 )]And a second chain end [ end (Re) 2 )]Independently selected from the group consisting of: -CR H 1 R H 2 -OC (=o) F, -C (=o) F, and-CR H 1 R H 2 F, wherein R is H 1 And R is H 2 Are identical or different from each other and are each independently H or C 1 -C 6 A hydrocarbon group;
the method comprises the following steps:
step (I): contacting the following in the presence of at least one fluorochemical:
-at least one perfluoro compound comprising at least two acyl fluoride groups [ compound (F) ]; and
at least one comprising at least two compounds of formula-CR H 1 R H 2 Hydrogenated compounds of the chloroformate group of-O-C (O) F [ Compound (H)]，
To provide a polymer comprising a partially fluorinated polyether backbone with two chain ends [ Polymer (FH) FOR )]Is used for the step of the mixture of (a),
wherein the backbone comprises one or more repeating units derived from the at least one compound (F) alternating with one or more repeating units derived from the at least one compound (H) and
wherein each of the chain ends, which are identical or different from each other, is selected from the group consisting of-CR H 1 R H 2 -OC (=o) F and a group-C (=o) F;
step (II): the polymer (FH) obtained in step (I) above FOR ) Heating at a temperature in excess of 120 ℃, preferably in the range from 130 ℃ to 210 ℃ and in the presence of a fluorochemical, typically in the presence of a fluorochemical comprising at least one of the following for a duration of at least 4 hours: (i) Having a MeF of y Wherein Me is a metal having a valence of y, y is 1 or 2, in particular NaF, caF 2 AgF, rbF, csF, KF; and (ii) has the formula NR HN 4 (alkyl) ammonium fluoride of F, wherein each R HN Are identical or different from one another, independently of one another, H or alkyl, in particular tetrabutylammonium fluoride,
thus realizing a polymer (FH) FOR ) Has the formula-CR H 1 R H 2 At least a part of the chain end of-OC (=O) F is attached to the group-CR H 1 R H 2 Thermal decomposition of F to provide a polymer mixture (FH CH2F ) Is carried out by a method comprising the steps of.
Then, in a second aspect, the invention relates to a polymer mixture (FH CH2F ) Wherein is of formula-CR H 1 R H 2 The concentration of chain ends of-F exceeds that of the formula-CR H 1 R H 2 -concentration of chain ends of OC (=o) F.
Other aspects and objects of the invention will appear from the detailed description below.
Detailed Description
For the purposes of this specification and the following claims:
use of parentheses around the sign or number of the logo, for example in expressions like "polymer mixture (PH FOR ) "etc., has the purpose of distinguishing only the symbol or number better from the rest of the text, and thus the parentheses may also be omitted;
the term "(per) fluoropolyether" is intended to mean one or more polyether polymers comprising a fully fluorinated or partially fluorinated backbone;
the term "perfluoropolyether" is intended to mean one or more polyether polymers comprising a fully fluorinated backbone.
Preferably, the compound (F) is a compound having the formula:
F-C(＝O)-R f -C(＝O)-F
wherein R is f Is a divalent perfluorinated linear or branched (oxy) alkylene chain, wherein the alkylene chain comprises from 1 to 10 carbon atoms and is optionally interrupted by one or more oxygen atoms.
More preferably, the perfluoro (oxy) alkylene is a linear alkylene, i.e. is formed by-CF 2 -a group consisting of sequences, possibly comprising one or more than one ether oxygen-O-.
More preferably, the perfluoro (oxy) alkylene contains from 1 to 5 carbon atoms, even more preferably from 1 to 4 carbon atoms.
According to a preferred embodiment, said compound (F) is selected from the group comprising:
(F-i)FC(O)-CF 2 -C(O)F；
(F-ii)FC(O)-CF 2 -CF 2 -C(O)F；
(F-iii)FC(O)-CF 2 -CF 2 -CF 2 -C(O)F；
(F-iv)FC(O)-CF 2 -CF 2 -CF 2 -CF 2 -C(O)F；
(F-v)FC(O)-CF 2 -O-CF 2 -C(O)F。
as mentioned above, the compound (H) is hydrogenated, i.e. the hydrogen atom saturates all the free valences on the carbon atoms of the compound, except for the chlorofluoroate group-CH 2 The fluorine atom of-OC (O) -F is present as such (as per).
Preferably, the compound (H) is a compound having the formula:
F-C(＝O)O-CR H 1 R H 2 -E H -CR H 1 R H 2 -OC(＝O)-F
wherein E is H Selected from the group consisting of a bond, -O-group, and a divalent linear or branched (oxy) alkylene group, wherein the (oxy group) Alkylene groups contain from 1 to 8 carbon atoms and are optionally interrupted by one or more ether oxygen atoms;
R H 1 and R is H 2 Each of which is the same or different from each other and is independently at each occurrence H or C 1 -C 6 A hydrocarbon group.
More preferably, said E H (oxy) alkylene of (a) is a linear (oxy) alkylene, i.e. is composed of-CH 2 -a group consisting of sequences, possibly comprising one or more than one ether oxygen-O-.
More preferably, the (oxy) alkylene contains from 1 to 10 carbon atoms, even more preferably from 1 to 6 carbon atoms, and still more preferably from 1 to 4 carbon atoms.
More preferably, R H 1 And R is H 2 Each of which is the same or different from each other and is independently at each occurrence H or C 1 -C 3 An alkyl group; more preferably H or-CH 3 The method comprises the steps of carrying out a first treatment on the surface of the Most preferably H.
Preferably, the compound (H) is selected from the group consisting of:
(H-j)F-C(O)-O-(CH 2 ) 2 -O-C(O)-F、
(H-jj)F-C(O)-O-(CH 2 ) 3 -O-C(O)-F、
(H-jjj)F-C(O)-O-(CH 2 ) 4 -O-C(O)-F、
(H-jv)F-C(O)-O-(CH 2 ) 5 -O-C (O) -F, and
(H-v)F-C(O)-O-(CH 2 ) 2 -O-(CH 2 ) 2 -O-C(O)-F。
although the molar ratio between the compound (H) and the compound (F) in step (I) of the process of the present invention is not particularly limited, it will generally be understood that this ratio is generally adjusted within 5.0:1.0 to 1.0:5.0, preferably within 2.0:1.0 to 1.0:2.0, more preferably within 1.3:1.0 to 1.0:1.3, and even more preferably within 1.1:1.0 to 1.0:1.1, meaning that the excess of acyl fluoride or chloroformate is generally Ji Zhiduo% by mole, preferably Ji Zhiduo 200,200% by mole, more preferably up to 30% by mole, even more preferably up to Ji Zhiduo 10% by mole.
As stated, step (I) of the process of the present invention is carried out in the presence of a fluorochemical compound, more preferably in the presence of a fluorochemical compound comprising at least one of the following: (i) Having a MeF of y Wherein Me is a metal having a valence of y, y is 1 or 2, in particular NaF, caF 2 AgF, rbF, csF, KF; and (ii) has the formula NR HN 4 (alkyl) ammonium fluoride of F, wherein each R HN Are identical or different from one another and are independently H or alkyl, in particular tetrabutylammonium fluoride.
The fluorine-containing compound may be a pure metal fluoride or pure (alkyl) ammonium fluoride as detailed above, or may be a compound, with the fluoride being supported on an inert carrier such as charcoal, alumina, silica, zeolite, or the like.
It will be generally understood that in step (I) of the process of the invention, the reaction between compound (F) and compound (H) is carried out by-CF, although other mechanisms may also explain the observed reactivity 2 -O - The formation of nucleophiles (by reaction of the fluoride with the acyl fluoride group of compound (F)) and its subsequent nucleophilic substitution on the chloroformate group of compound (H), in which carbon dioxide and fluoride are released, takes place.
As a result, the fluorochemical can be used in catalytic amounts, it being understood that the fluorochemical anion will not be substantially consumed in step (I).
Cesium fluoride (CsF), potassium fluoride (KF), silver fluoride (AgF), rubidium fluoride (RbF) and tetra-n-butyl ammonium fluoride are preferred fluorine-containing compounds which can be used in step (I) of the process of the invention.
Preferably, step (I) is carried out in the presence of a solvent, more preferably in the presence of a polar aprotic solvent, although embodiments in which no solvent is used and compounds (F) and (H) are used as reactive medium are also encompassed by the process of the invention.
When used, the polar aprotic solvent is preferably selected from the group comprising, more preferably consisting of: dimethoxyethane (glyme), bis (2-methoxyethyl) ether (diglyme), triethylene glycol dimethyl ether (triglyme), tetraethylene glycol dimethyl ether (tetraglyme), tetrahydrofuran, acetonitrile, dimethyl sulfoxide, dimethylformamide, and ethylene polyoxide dimethyl ether. Tetraglyme and acetonitrile are more preferred.
Step (I) may be performed by adding the compound (F) to the compound (H), or vice versa, by adding the compound (H) to the compound (F). According to a preferred embodiment, the compound (F) and the compound (H) are added to the reaction environment and the reaction is then triggered by, for example, increasing the temperature and/or adding the fluorine source.
Step (I) is generally carried out at a temperature of at least 60 ℃, preferably at least 80 ℃, more preferably at least 90 ℃, even more preferably at least 110 ℃.
The upper limit of the reaction temperature in step (I) is not particularly limited; however, it will generally be appreciated that step (I) will be carried out at a temperature lower than that of step (II) and typically at most 120 ℃.
Preferably, after step (I), the polymer mixture (FH FOR ) The main chain of the polymer chain of (2) is mainly composed of a polymer chain having the formula (FH Unit cell ) Sequence composition of repeating units of (a):
-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O]-(FH unit cell )
Wherein the method comprises the steps of
R f Has the same meaning as defined above for compound (F),
E H 、R H 1 and R is H 2 Has the same meaning as defined above for compound (H).
As above for characterizing the polymer mixture (FH FOR ) The expression "consisting essentially of … …" is intended to mean that the polymer chain backbone of (a) is free of repeating units (FH Unit cell ) In addition to the sequences of (2), the chains may also contain minor defects and/or pseudo-single species which may result from side reactionsThe meta (spinious unit) will be understood to be in such an amount that the polymer mixture (FH) is not substantially modified FOR ) For example with respect to the polymer mixture (FH FOR ) The total amount of repeating units of the polymer chain is less than 1% by mole.
Said polymer (FH) FOR ) The number average molecular weight of (a) is from 210 to 50,000, preferably from 380 to 30,000, more preferably from 450 to 8,000, and even more preferably from 500 to 3,000.
Polymer mixture (FH) FOR ) Generally a mixture comprising variable amounts of any compound having (preferably consisting essentially of) the formula:
(1)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) FOR-FOR )]；
(2)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C (O) -F [ type (FH) COF-FOR )]
(3)
F-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Where n ', n ", and n'" are integers such that the polymer (FH FOR ) The molecular weight of (a) is within the limits listed above, i.e., from 210 to 50,000, preferably from 380 to 30,000, more preferably from 450 to 8,000, and even more preferably from 500 to 3,000; and R is f 、E H 、R H 1 And R is H 2 Having the meaning as detailed above.
The expression "consisting essentially of … …", when used in conjunction with the expression to characterize the production of the polymer mixture (FH FOR ) "Polymer mixture (FH) FOR ) "in combination" is understood to mean that further compounds may be present in the mixture, which may form as a result of side reactions or as a result of the presence of impurities and/or spurious components.
It will be clear to the person skilled in the art that when the reaction conditions of step (I) are controlled, the compounds (FH FOR-FOR )、(FH COF-FOR ) Sum (FH) COF-COF ) The stoichiometry of the reaction and the reactivity of the compounds (H) and (F) are notably taken into account.
However, it will be appreciated in general that the process of the invention may be adapted to produce a composition comprising a compound of any Formula (FH) as detailed above, notably with respect to the relative molar amounts of compound (F) and compound (H), taking into account the reactivity of the-COF and-O-C (O) -F groups under different reaction conditions FOR-FOR )、(FH COF-FOR ) Sum (FH) COF-COF ) Polymer mixture of compounds (FH) FOR ) In such an amount as to have the formula (FH COF-FOR ) The concentrate of the compound of (2) is a polymer mixture (FH FOR ) Is a major component of (a) a compound.
According to these examples, the polymer mixture (FH FOR ) Including those described in detail above with any of (FH FOR-FOR )、(FH COF-FOR ) Sum (FH) COF-COF ) In an amount such that it has the formula-CR H 1 R H 2 The concentration of chain ends of-OC (=O) F is relative to the polymer mixture (FH FOR ) At least 40 mole%, preferably at least 45 mole%, and more preferably at least 50 mole%, and/or up to 75 mole%, preferably up to 60 mole%, of the total moles of chain ends in (a), wherein R H 1 And R is H 2 Having the meaning as detailed above.
Similarly, the process parameters of step (I) of the method of the invention may be adjusted to ensure that the method of the invention produces a composition comprising a composition having any of the Formulas (FH) as detailed above FOR-FOR )、(FH COF-FOR ) Sum (FH) COF-COF ) Polymer mixture of compounds (FH) FOR ) In such an amount as to have the formula (FH FOR-FOR ) The concentrate of the compound of (2) is a polymer mixture (FH FOR ) Is a major component of (a) a compound.
According to these examples, the polymer mixture (FH FOR ) Including those described in detail above with any of (FH FOR-FOR )、(FH COF-FOR ) Sum (FH) COF-COF ) In an amount such that it has the formula-CR H 1 R H 2 The concentration of chain ends of-OC (=O) F is relative to the polymer mixture (FH FOR ) More than 60 mole%, preferably at least 65 mole%, and more preferably at least 70 mole% of the total moles of chain ends in (a), wherein R H 1 And R is H 2 Having the meaning as detailed above.
More generally, as mentioned, in step (II) of the process of the invention, the polymer mixture (FH FOR ) Has the formula-CR H 1 R H 2 At least a part of the chain end of-OC (=O) F is attached to the group-CR H 1 R H 2 Thermal decomposition of-F takes place, and R H 1 And R is H 2 Having the meaning detailed above.
Step (II) may be a separate step from step (I) or may occur simultaneously with step (I) because the reaction between polymer (F) and polymer (H) is performed according to the temperature in step (I).
However, in order to achieve a formula-CR H 1 R H 2 Chain end to group-CR of-OC (=O) F H 1 R H 2 Substantial thermal decomposition of F, it is essential for step (II) to include heating at a temperature exceeding 120℃and preferably at least 130℃and even more preferably at least 140℃for at least 4 hoursIs not shown, is not shown.
As mentioned, in said step (II), a fluorine-containing compound must be present for effectively catalyzing said catalyst having the formula-CR H 1 R H 2 Chain end to group-CR of-OC (=O) F H 1 R H 2 -said thermal decomposition of F.
The fluorine-containing compound may be the same compound as used in step (I) or may be a different compound. In general, the following embodiments are preferred: wherein step (I) and step (II) are carried out in the presence of the same fluorochemical compound, and wherein said fluorochemical compound is added to the reaction mixture used in step (I) and is thus present in the polymer mixture (FH FOR ) Is a kind of medium.
In the polymer mixture (FH) FOR ) In the case where the amount of the fluorine-containing compound present is not appropriately used for optimizing the thermal decomposition conditions in the step (II), it is possible to:
isolation of the Polymer mixture (FH) FOR ) At least a portion of the fluorochemical compound present in the reaction mixture in order to prevent its amount from being too high at the end of step (I); or alternatively
To the polymer mixture (FH FOR ) At least a portion of the additional fluorine-containing compound is added to prevent its amount from being too low at the end of step (I).
As mentioned, step (II) of the process of the invention achieves a polymer mixture (FH FOR ) Has the formula-CR H 1 R H 2 At least a part of the chain end of-OC (=O) F is attached to the group-CR H 1 R H 2 Thermal decomposition in order to obtain a polymer mixture (FH CH2F )。
The polymer mixture (FH CH2F ) The number average molecular weight of (c) is advantageously from 210 to 50000, preferably from 380 to 30 000, more preferably from 450 to 8 000, and even more preferably from 500 to 3 000.
Polymer mixture (FH) CH2F ) Generally a mixture comprising variable amounts of any compound having (preferably consisting essentially of) the formula:
(a)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 f [ type (FH) CH2F-CH2F )]；
(b)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]；
(c)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) FOR-FOR )]；
(d)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) CH2F-FOR )]；
(e)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C (O) -F [ type (FH) COF-FOR )]
(f)
F-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Where n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (2) is within the limits listed above, and wherein R f 、E H 、R H 1 And R is H 2 As described in detail above.
Those skilled in the art will recognize that the above compounds (c), (d), (e) and (f) are indeed polymer mixtures (FH FOR ) Is representative of an unreacted (c, e, f) component or a partially reacted (d) component.
Among those compounds, the polymer mixture (FH CH2F ) In (a):
-having the formula (FH CH2F-CH2F ) The concentration of the compound of Formula (FH) is higher than that of the compound of formula (FH FOR-FOR ) The concentration of the compound of (a); and/or
-having the formula (FH COF-CH2F ) The concentration of the compound of Formula (FH) is higher than that of the compound of Formula (FH) COF-FOR ) The concentration of the compound of (a).
Typically, the conditions in step (II) are adjusted so as to cause a reaction of the compound of formula-CR relative to that produced as in step (I) H 1 R H 2 A polymer mixture (FH) with a total amount of chain ends of-OC (=o) F of more than 50%, preferably more than 60%, more preferably more than 70% FOR ) Has the formula-CR H 1 R H 2 -OC(Thermal decomposition of chain ends of =o) F, wherein R H 1 And R is H 2 Having the meaning as detailed above.
The applicant has noted that by adjusting the heating temperature and the heating duration in step (II), the group-OC (=o) F to group-CR can be obtained H 1 R H 2 Complete or partial conversion of F, wherein R H 1 And R is H 2 Having the meaning as detailed above.
Another aspect of the invention is a polymer mixture (FH CH2F ) Wherein is of formula-CR H 1 R H 2 F (preferably of formula-CH) 2 The concentration of chain ends of-F) exceeds that of the formula-CR H 1 R H 2 -OC (=o) F (preferably of formula-CH 2 -concentration of chain ends of OC (=o) F, wherein R H 1 And R is H 2 Having the meaning as detailed above.
According to certain preferred embodiments, the process of the invention can be adjusted to provide a polymer mixture (FH CH2F ) The polymer mixture comprises an amount of a polymer having the formula (FH COF-CH2F ) Compounds (F-CR) H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C(O)-F，
Wherein E is H 、R f 、n**、R H 1 And R is H 2 Has the meaning as detailed above in an amount relative to a compound having the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 60 mole%, preferably at least 70 mole%, more preferably at least 80 mole% of the total moles of compounds of (a). We refer to such mixtures as poly(s)Mixture of compounds (FH) CH2F MONO )。
To produce a mixture (FH CH2F MONO ) The molar ratio between compound (H) and compound (F) in step (I) will be adjusted to provide a mixture (FH FOR ) (referred to herein as a polymer mixture (FH) FOR MONO ) The mixture comprising a compound having the Formula (FH) COF-FOR ) Compound F-C (O) -OCR of (C) H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C (O) -F, wherein E H 、R f 、n”、R H 1 And R is H 2 Has the meaning as detailed above in an amount relative to a compound having the formula (FH FOR-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 60 mol%, preferably at least 70 mol%, more preferably at least 80 mol%, of the total moles of compounds of (a) which, under the appropriate conditions, will produce said mixture (FH CH2F MONO )。
According to other embodiments, the process of the invention can be adjusted to provide a polymer mixture (FH CH2F ) The polymer mixture comprises an amount of a polymer of the formula (FH CH2F-CH2F ) Compound F-CR of (2) H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 F, wherein E H 、R f 、n*、R H 1 And R is H 2 Has the meaning as detailed above in an amount of phaseFor a sample having the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 60 mole%, preferably at least 70 mole%, more preferably at least 80 mole% of the total moles of compounds of (a). We refer to this mixture as a polymer mixture (FH CH2F Neutral )。
To produce a mixture (FH CH2F Neutral ) The molar ratio between compound (H) and compound (F) in step (I) will be adjusted to provide a mixture (FH FOR ) (referred to herein as a polymer mixture (FH) FOR Neutral ) The mixture comprising a compound having the Formula (FH) FOR-FOR ) Is a compound of formula (I)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F, wherein E H 、R f 、n’、R H 1 And R is H 2 Has the meaning as detailed above in an amount relative to a compound having the formula (FH FOR-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 60 mol%, preferably at least 70 mol%, more preferably at least 80 mol%, of the total moles of compounds of (a) which, under the appropriate conditions, will produce said mixture (FH CH2F Neutral )。
According to certain preferred embodiments, the catalyst is selected from the group consisting of a catalyst having the formula-CR as produced in step (I) H 1 R H 2 The total amount of chain ends of-OC (=O) F, step (II) of the process of the invention causes the polymerization mixture (FH FOR ) Is of the formula-CR H 1 R H 2 Thermal decomposition of the chain end of OC (=o) F. In other words, this means for determining and quantifying the polymer mixture (FH CH2F ) Characterization of the chain ends of (C)No significant amount of-CR can be detected by surgery H 1 R H 2 -OC (=o) F groups, or in other words, their concentration is lower than the limit of detection of the characterization technique, whereas R H 1 And R is H 2 Having the meaning as detailed above.
According to these involve complete thermal decomposition (producing no detectable amount of-CR H 1 R H 2 In a preferred embodiment of the-OC (=O) F group, the polymer mixture (FH CH2F ) Preferably a mixture comprising variable amounts of any compound having (preferably consisting essentially of) the formula:
(a’)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 f [ type (FH) CH2F-CH2F )]；
(b’)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]The method comprises the steps of carrying out a first treatment on the surface of the And
(e’)
F-C(O)R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Where n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (a) is from 210 to 50,000, preferably from 380 to 30,000, more preferably from 450 to 8,000, and even more preferably from 500 to 3,000, and wherein E H 、R f 、R H 1 And R is H 2 Having the meaning as detailed above.
According to certain embodiments of the invention, the process as detailed above comprises a further step (III) comprising reacting the polymer mixture (FH CH2F ) And to enable at least partial fluorination of the polymer mixture (FH CH2F ) Is contacted with a fluorine source to obtain a fluorinated polymer mixture (FF) CF3 )。
Advantageously, the polymerization is carried out by means of a polymer mixture (FH CH2F ) Is derived from the fluorination of the compound (H) as described in detail above H 1 R H 2 -E H -CR H 1 R H 2 - (wherein E) H 、R H 1 And R is H 2 With the meaning indicated above) at least a portion of the hydrogen atoms are replaced by fluorine atoms. According to a preferred embodiment, substantially all hydrogen atoms of said moiety are replaced by fluorine atoms in step (III), such that said moiety-CR H 1 R H 2 -E H -CR H 1 R H 2 -conversion to a compound of formula-CR F 1 R F 2 -E F -CR F 1 R F 2 -a group wherein:
-E F a perfluoro (oxy) alkylene selected from the group consisting of a bond, -O-group and a divalent straight or branched chain, wherein the perfluoro (oxy) alkylene comprises from 1 to 8 carbon atoms and is optionally interrupted by one or more ether oxygen atoms; and is also provided with
-R F 1 And R is F 2 Each of which is the same or different from each other and is independently F or C 1 -C 6 Fluorocarbon groups, preferably F or C 1 -C 3 Perfluoroalkyl, more preferably F or-CF 3 Most preferably F.
Preferably, the fluorine source in step (III) is a gas containing molecular fluorine. More preferably, the fluorine source is fluorine gas (F 2 )。
Advantageously, the fluorine source in step (III) is used in combination with a diluent gas, preferably selected from inert gases such as helium and nitrogen.
Advantageously, in step (III), the halogenated olefin can be reacted with a polymer mixture (FH CH2F ) Is contacted with a fluorine source in order to advantageously produce a promoting polymer mixture (FH CH2F ) Fluorinated fluoro groups of (a). The halogenated olefin may be selected from, for example, tetrafluoroethylene (TFE), hexafluoro-propylene (HFP), octafluorobutene, perfluoropentene, perfluorohexene, perfluoroheptene, perfluorooctene, perfluorocyclobutene, perfluorocyclopentene, perfluorocyclohexene, chlorotrifluoroethylene (CTFE), dichlorodifluoroethylene, chloropentafluoropropene, perfluorobutadiene, perfluoro-methyl vinyl ether, perfluoro-ethyl vinyl ether, perfluoro-propyl vinyl ether; CF (compact flash) 3 Oclc=cclf, trichloroethylene, tetrachloroethylene, dichloroethylene isomers; fluorodioxoles (fluorodioxoles).
In the examples, in which fluorination causes a polymer mixture (FH CH2F ) Substitution of substantially all hydrogen atoms, after step (III), of the polymer mixture (FF CF3 ) The main chain of the polymer chain of (2) is mainly composed of a polymer chain having the formula (FF) Unit cell ) Sequence composition of repeating units of (a):
-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]-(FF unit cell )
Wherein the method comprises the steps of
-R f Has the same meaning as defined above for compound (F),
-E F selected from the group consisting of a bond, -O-group and a divalent linear or branched perfluoro (oxy) alkylene group, wherein the perfluoro (oxy) alkylene group contains from 1 to 8 carbon atoms and is optionally substituted with one or more than oneAn interruption of the ether oxygen atom; and is also provided with
-R F 1 And R is F 2 Each of which is the same or different from each other and is independently F or C 1 -C 6 Fluorocarbon groups, preferably F or C 1 -C 3 Perfluoroalkyl, more preferably F or-CF 3 Most preferably F.
According to a first variant, the fluorination step (III) is carried out in a polymer mixture (FH) as obtained in step (II) CH2F ) Possibly after standard isolation/purification steps.
According to this first variant of step (III), in general, the polymer mixture (FH) having the formula-C (O) -F or the formula-O (CO) -F CH2F ) The terminal chains of the polymer compound of (a) will not be affected by fluorination in step (III); in contrast, in the polymer chain, and of formula-CR H 1 R H 2 In both end groups of F, the C-H bonds will be essentially replaced, these bonds will be converted to-CR F 1 R F 2 F group, wherein R H 1 、R H 2 、R F 1 And R F 2 Having the meaning as detailed above.
In the polymer mixture (FH) CH2F ) It is generally preferred to avoid exposing a compound of that mixture in which one or both chain ends are one or more acyl fluoride-C (O) -F groups to conditions in which hydrolysis may occur.
Indeed, under hydrolytic conditions, the-C (O) F group may yield the corresponding carboxylic acid group-COOH, which may be unstable under the fluorination conditions of step (III).
More precisely, the compounds:
(b)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C(O)-f [ type (FH) COF-CH2F )]；
(e)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C (O) -F [ type (FH) COF-FOR )]
(f)
F-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Where the treatment exposes the mixture to moisture, partial (or even complete) conversion of the corresponding hydrolyzed acid derivative listed below may be experienced during the treatment of step (II):
(b hydrolysis )
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -OH [ type (FH) COOH-CH2F )]；
(e Hydrolysis )
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 Rf-C (O) -OH [ Formula (FH) COOH-FOR )]
(f Hydrolysis )
HO-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -OH [ type (FH) COOH-COOH )]
Where n, n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (2) is within the limits listed above, and wherein R f 、E H 、R H 1 And R is H 2 As described in detail above.
During fluorination, bonded to part R f The terminal carboxyl groups on the fluorinated carbon of (2) can be decarboxylated to release CO 2 And HF, thereby creating additional "non-functional" end groups.
In particular, the hydrolyzed acid derivatives listed below:
(b hydrolysis )
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -OH [ type (FH) COOH-CH2F )]；
(e Hydrolysis )
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O]n”-CF 2 -R f -C (O) -OH [ type (FH) COOH-FOR )]
(f Hydrolysis )
HO-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -OH [ type (FH) COOH-COOH )]
Where n, n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (2) is within the limits listed above, and wherein R f 、E H 、R H 1 And R is H 2 As is described in detail above,
partial (or even complete) decarboxylation of the corresponding fluorinated neutral derivative listed below may be experienced during the fluorination step (III):
(b” decarboxylation )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -F [ formula (FF) F-CF3 )]；
(e” Decarboxylation )
F-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]n”-CF 2 -R f -F [ formula (FF) F-FOR )]
(f” Decarboxylation )
F-R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n’” -CF 2 -R f -F [ formula (FF) F-F )]。
According to a first variant of step (III), the polymer mixture (FF CF3 ) Generally a mixture comprising variable amounts of any compound having (preferably consisting essentially of) the formula:
(a”)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n* -CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -F [ formula (FF) CF3-CF3 )]；
(b”)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]n**-CF 2 -R f -C (O) -F [ formula (FF) COF-CF3 )]；
(c”)
F-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n' -C (O) -F [ formula (FF) FOR-FOR )]；
(d”)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]n' -C (O) -F [ formula (FF) CF3-FOR )]；
(e”)
F-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n” -CF 2 -R f -C (O) -F [ formula (FF) COF-FOR )]
(f”)
F-C(O)R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n’” -CF 2 -R f -C (O) -F [ formula (FF) COF-COF )]；
And optionally further comprising one or more of the following compounds:
(b” decarboxylation )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -F [ formula (FF) F-CF3 )]；
(e” Decarboxylation )
F-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n” -CF 2 -R f -F [ formula (FF) F-FOR )]
(f” Decarboxylation )
F-R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n’” -CF 2 -R f -F [ formula (FF) F-F )]，
Wherein n, n ', n ", and n'" are integers such that the polymer mixture (FF CF3 ) The molecular weight of (2) is from 210 to 50,000, preferably from 380 to 30,000, more preferably from 450 to 8,000, and even more preferably from 500 to 3,000, and wherein R f 、E F 、R F 1 And R F 2 As described in detail above.
According to a first variant of step (III), in the embodiment in which the thermal decomposition in step (II) is carried out to completion such that no residual chloroformate groups are present, the polymer mixture (FF CF3 ) Preferably a mixture comprising variable amounts of any compound having (preferably consisting essentially of) the formula:
(a’ v )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n* -CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -F [ formula (FF) CF3-CF3 )]；
(b’ v )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -C (O) -F [ formula (FF) COF-CF3 )]The method comprises the steps of carrying out a first treatment on the surface of the And
(f’ v )
F-C(O)R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n’” -CF 2 -R f -C (O) -F [ formula (FF) COF-COF )]；
Optionally:
(b” decarboxylation )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -F [ formula (FF) F-CF3 )]；
(f” Decarboxylation )
F-R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]n’”-CF 2 -R f -F [ formula (FF) F-F )]，
Wherein n, and n' "are integers such that the polymer mixture (FF CF3 ) The molecular weight of (a) is from 210 to 50,000, preferably from 380 to 30,000, more preferably from450 to 8 000, and even more preferably from 500 to 3 000, and wherein R f 、E F 、R F 1 And R F 2 As described in detail above.
According to a first variant of step (III), according to certain preferred embodiments, the process of the invention can be adapted to provide a polymer mixture (FF CF3 ) The polymer mixture comprises an amount of a polymer having the formula (FF COF-CF3 ) Is a compound of formula (I)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -C (O) -F (wherein n is such that the molecular weight of the compound is from 210 to 50 000, preferably from 380 to 30 000, more preferably from 450 to 8 000, and even more preferably from 500 to 3 000, and wherein R f 、E F 、R F 1 And R F 2 As described above) in an amount relative to a composition having the formula (FF) CF3-CF3 ) (FF) COF-CF3 ) (FF) FOR-FOR ) (FF) COF-FOR ) And Formula (FF) COF-COF ) At least 60 mole%, preferably at least 70 mole%, more preferably at least 80 mole% of the total moles of compounds of (a). We refer to this mixture as a polymer mixture (FF CF3 MONO )。
According to a first variant of step (III), the mixture (FF CF3 MONO ) Can be prepared from a polymer mixture (FH CH2F MONO ) Obtained by fluorination in step (III) as detailed above under suitable conditions in order to advantageously ensure extensive/thorough fluorination and replacement of substantially all C-H bonds by C-F bonds.
According to a first variant of step (III), but according to other embodiments, the process of the invention can be adapted to provide a polymer mixture (FF CF3 ) The polymer mixture comprises a certain amount ofAs detailed above, of the formula (FF CF3-CF3 ) Is a compound of formula (I)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n* -CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -F (wherein n is such that the molecular weight of the compound is from 210 to 50,000, preferably from 380 to 30,000, more preferably from 450 to 8,000, and even more preferably from 500 to 3,000, and wherein R f 、E F 、R F 1 And R is F 2 As described above) in an amount relative to a composition having the formula (FF) CF3-CF3 ) (FF) COF-CF3 ) (FF) FOR-FOR ) (FF) COF-FOR ) And (FF) COF-COF ) At least 60 mole%, preferably at least 70 mole%, more preferably at least 80 mole% of the total moles of compounds of (a). We refer to this mixture as a polymer mixture (FF CF3 Neutral )。
According to a first variant of step (III), in order to produce a polymer mixture (FF CF3 Neutral ) The mixture as described in detail above (FH CH2F Neutral ) In step (III) fluorination conditions are subjected to ensure extensive/thorough fluorination and replacement of substantially all of the C-H bonds by C-F bonds.
According to a second variant, the polymer mixture (FH) as obtained from step (II) is subjected to a step (III) of fluorination CH2F ) Undergo at least one step (III) of derivatization of the end groups of the acyl fluoride and/or chlorofluoroate, modifying the chemical nature thereof A ) To produce a polymer mixture (FH CH 2F-derivatives ). It is generally understood that the polymerization reaction is carried out in the presence of the polymer mixture (FH) initially contained as obtained in step (II) CH2F ) In the polymer mixture (FH) CH 2F-derivatizationArticle (B) ) Will become more stable, notably towards hydrolysis and decarboxylation.
In particular, in this second variant, according to certain embodiments, in step (III A ) In the polymer mixture (FH) CH2F ) Can be prepared under esterification conditions under the formula R h Reaction in the presence of an alcohol of OH (wherein R h Is C 1 -C 3 Hydrocarbyl radicals, e.g. CH 3 、C 2 H 5 、C 3 H 7 Preferably C 2 H 5 ) The method comprises the steps of carrying out a first treatment on the surface of the To provide a polymer mixture (FH CH 2F-ester/carbonate ) The polymer mixture (FH CH 2F-ester/carbonate ) Generally a mixture comprising variable amounts of any compound having (preferably consisting essentially of) the formula:
(a^)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 f [ type (FH) CH2F-CH2F )]；
(b^)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C(O)-O-R h [ type (FH) esters-CH 2F )]；
(c^)
R h O-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C(O)-O-R h [ type (FH) Carbonate-carbonate )]；
(d^)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C(O)-O-R h [ type (FH) CH 2F-carbonates )]；
(e^)
R h O-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C(O)-OR h [ type (FH) Ester-carbonates )]
(f^)
R h O-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C(O)-OR h [ type (FH) Ester-ester )]
Where n, n ', n ", and n'" are integers such that the polymer mixture (FH CH 2F-ester-carbonate ) The molecular weight of (2) is from 210 to 50,000, preferably from 380 to 30,000, more preferably from 450 to 8,000, and even more preferably from 500 to 3,000, and wherein R f 、E H 、R h 、R H 1 And R is H 2 As described in detail above.
Polymer mixture (FH) CH2F ) Is notably effective in substantially avoiding the presence of derivatives having COOH end groups, which can undergo decarboxylation under fluorination step (III).
According to this second variant, the fluorination step (III) as described in detail above produces a polymer mixture (FF CF3 ester carbonate ) The polymer mixture comprises (preferably consists essentially of) variable amounts of any compound having the formula:
(a^ f )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n* -CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -F [ formula (FF) CF3-CF3 )]；
(b^ f )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -C(O)-OR hF [ type (FF) ester-CF 3 )]；
(c^ f )
R hF -O(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n' -C(O)-OR hF [ type (FF) Carbonate-carbonate )]；
(d^ f )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]n'-C(O)-OR hF [ type (FF) CF 3-carbonic acid ester )]；
(e^ f )
R hF O-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]n”-CF 2 -R f -C(O)-OR hF [ type (FF) Ester-carbonates )]
(f^ f )
R hF O-C(O)R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n’” -CF 2 -R f -C(O)-OR hF [ type (FF) Ester-ester )]
Wherein n, n ', n ", and n'" are integers such that the polymer mixture (FF CF3 ) The molecular weight of (2) is from 210 to 50,000, preferably from 380 to 30,000, more preferably from 450 to 8,000, and even more preferably from 500 to 3,000, and wherein R f 、E F 、R F 1 And R F 2 Is as described in detail above, and R hF Is C 1 -C 3 Fluorocarbon groups, e.g. CF 3 、C 2 F 5 、C 3 F 7 Preferably C 2 F 5 。
Polymer mixture (FH) CH2F )、(FH CH 2F-ester-carbonate )、(FF CF3 ester carbonate ) And%FF CF3 ) May be used as such or may be further modified using:
(i) Reactivity of-C (O) F [ as in mixtures (FH) CH2F ) Neutralization as in mixtures (FF CF3 ) In (a) and (b); or as in mixtures (FH CH 2F-ester-carbonate ) Neutralization as in mixtures (FF CF3 ester carbonate ) those-C (O) -F groups as esters]A kind of electronic device
(ii) Reactivity of-O-C (O) -F groups [ as in mixtures (FH) CH2F ) as-CR H 1 R H 2 -OC (O) -F groups are present; such as in mixtures (FH CH 2F-ester-carbonate ) Neutralization in the mixture (FF CF3 ester carbonate ) As a carbonate; or as in a mixture (FF CF3 ) as-CR F 1 R F 2 those-O-C (O) -F groups of-OC (O) -F groups ]
To produce different chain ends and/or may be subjected to a plurality of further separation steps in order to separate particular components thereof, possibly in high yields.
Either chemical type may be applied to these groups; in particular, the-C (O) F groups may undergo hydrolysis/esterification reactions, yielding carboxyl-type end groups, including carboxylic acids, esters, amides, acyl halides other than fluoride groups, or may react with different reactants starting from said acyl/carboxyl-type end groups, for example as described in US 3810874 (minnesota mining & manufacturing company (MINNESOTAMINING AND MANUFACTURING COMPANY)) 14/05/1974.
Thus, for example, a polymer mixture (FH CH2F ) Has a Formula (FH) COF-CH2F ) Of the compounds F-CH 2 -E H -CH 2 -O-[CF 2 -R f -CF 2 O-CH 2 -E H -CH 2 -O] n** -CF 2 -R f -C (O) -F is modified to have Formula (FH) A-CH2F ) Has the formula F-CH 2 -E H -CH 2 -O-[CF 2 -R f -CF 2 O-CH 2 -E H -CH 2 -O] n** -CF 2 -R f -a compound of formula (i), wherein n is H And R is f Has the meaning defined above, and A is of the formula-X a YZ b Wherein:
-X is a multivalent, preferably divalent, linking organic group, preferably selected from the group consisting of: -CONR-, -COO-, -COS-, -CO-, and a group of any formula
-a is zero or one;
-b is an integer from 1 to 3;
r is hydrogen, (e.g., CH) 3 、-CH 2 CF 3 、-C 6 H 13 ) Aryl groups having less than 13 carbon atoms (e.g., -C) 6 H 5 、-C 6 H 4 CH 3 ) or-YZ b A group;
y is a bond free of ethylenic unsaturation or a multivalent linking organic group, such as alkylene (e.g., -CH 2 -、-C 2 H 4 (-), oxa-alkylene (e.g., -CH) 2 OCH 2 (-) cycloalkylene radicals (e.g. -C-C) 6 H 10 (-), thio-alkylene (e.g., -CH) 2 SCH 2 (-), arylene (e.g. -C) 6 H 4 (-), or combinations thereof, such as arylalkylene and alkylarylene;
-Z is a functional group which may notably undergo electrophilic, nucleophilic or radical reactions and which may notably be selected from the group consisting of: -OH, -SH, -SR', -NR 2 '、-CO 2 H、-SiR' d Q 3-d 、-CN、-NCO、>C＝C<、-CO 2 R’、-OSO 2 CF 3 、-OCOCI、-OCN、-N(R')CN、-(O)COC(O)-、-N＝C、-I、-CHO、-CH(OCH 3 ) 2 、-SO 2 CI、-C(OCH 3 )＝NH、-C(NH 2 )＝NH、-C 6 H 4 OC 6 H 4 -Q、-OCR 1 R 2 R f 、
Wherein R' is hydrogen, aryl, or C 1 -C 6 An alkyl group; q is halogen, -OR ', -OCOR', OR-ch=ch 2 The method comprises the steps of carrying out a first treatment on the surface of the And d is or an integer from 1 to 3; r is R 1 Is hydrogen or C 1 -C 6 (fluoro) alkyl, R 2 Is hydrogen or C 1 -C 6 An alkyl group; and R is f Is C 1 -C 6 (fluoro) alkyl.
Similarly, a polymer blend (FF CF3 ) Has the formula (FF) COF-CF3 ) Compound F of (2) 3 C-E F -CF 2 -O-[CF 2 -R f -CF 2 O-CF 2 -E F -CF 2 -O] n** -CF 2 -R f Modification of-C (O) -F to have formula F 3 C-E F -CF 2 -O-[CF 2 -R f -CF 2 O-CF 2 -E F -CF 2 -O] n** -CF 2 -R f -a compound of formula (i), wherein E F 、n**、R f And a is as detailed above.
Similarly, either chemical type may be applied to the-O-C (O) F group. In particular, the-CH 2 -OC (O) -F and-CF 2 the-OC (O) -F group may undergo hydrolysis/esterification reactions, yielding-CH respectively 2 -OC (O) -OR (wherein R is (halo) hydrocarbyl); or-C (O) -R (wherein R is (halo) hydrocarbyl); the acid/ester or carbonate acid/ester groups may further react with different reactants starting from said acyl/carboxyl end groups, as described notably in US 3810874 (minnesota mining and manufacturing company) 14/05/1974, and as detailed above.
Notably, the polymer mixture as such or further modified as detailed above (FH CH2F )、(FH CH 2F-ester-carbonate )、(FF CF3 ester carbonate ) Sum (FF) CF3 ) Can be used for manufacturing additives for plastic and glass coatings.
The description should take precedence if the disclosure of any patent, patent application, or publication incorporated by reference into this application conflicts with the description of the application to the extent that the term "unclear".
The invention will be explained in more detail hereinafter by means of examples contained in the experimental section below; these examples are illustrative only and are in no way to be construed as limiting the scope of the invention.
Experimental part
Method
The number average molecular weight (Mn) was determined by NMR analysis 19 F-NMR 1 H-NMR).
Material
The dry CsF powder (title 99.9%) was obtained from Aldrich co.
EXAMPLE 1 monofunctional Poly-C 3 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of 1)
In a Parr autoclave (600 ml) equipped with a mechanical stirrer and a pressure sensor, dry CsF powder (52.27 g,0.34 mol.), chloroformate F (O) C-O (CH) 2 ) 3 O-C (O) F (115.68 g,0.69 mol.) and anhydrous tetraethyleneglycol dimethyl ether (150 g) were charged into a dry box under a nitrogen atmosphere. At-196℃at 10 -5 After removal of the non-condensable gases by vacuum at mbar, the perfluoromalonyl fluoride FC (O) -CF 2 C (O) F (99.10 g,0.69 mol) was condensed in an autoclave at liquid nitrogen temperature. The reaction mixture was heated at 120 ℃ by heating mantle and kept at this temperature for 8 hours under mechanical stirring. During this time due to CO 2 The pressure increase was monitored. After the reaction was completed, the autoclave was cooled to room temperature, and the gaseous product (CO 2 HF) was eliminated and bubbled into 10% NaOH solutionIn liquid (600 cc). The fluorinated phase inside the autoclave was recovered and the reaction mixture was filtered under pressure through a PTFE filter (0.45 mm) to remove most of the CsF catalyst. Of crude mixtures 1 H-NMR 19 F-NMR analysis shows the inclusion of end groups-CF 2 C(O)F(38％mol.)、-CH 2 -OC (O) F (55% mol.) and-CH 2 F (7% mol.) formation of partially fluorinated polyether polymers, the presence of these groups being indicative of certain-CH groups 2 The characteristic partial thermal decomposition of the-OC (O) F group.
Step (b): providing a polymer mixture (FH CH2F Thermal decomposition of 1)
The obtained product was poured into a glass flask equipped with a Claisen water condenser and heated in the presence of the remaining CsF in a nitrogen atmosphere over 8 hours ranging from 140 ℃ to 200 ℃ to convert the chloroformate groups to neutral groups-CH 2 F and simultaneously purified by fractional distillation to remove solvent and byproducts.
At the end of the heating step, 92.0g of the final polymer mixture (FH CH2F -1) the polymer mixture comprises a majority of monofunctional derivatives (having-COF and-CH 2 F end groups) and has a number average Molecular Weight (MW) equal to 1300 and contains groups-COF and groups-CH in an average amount of 44% mol% 2 F, e.g. by 1 H-NMR 19 F-NMR analysis.
Step (c): providing a polymer mixture (FF CF3 Perfluorinated reactions of-1), followed by hydrolysis with ethanol
25.0g of the polymer mixture obtained in step (b) was diluted in 130g of 1,2,3, 4-tetrachlorohexafluorobutane and loaded into 250ml of a stainless steel reactor equipped with a mechanical stirrer, two inlet pipes, thermocouple and outlet pipe. While maintaining the reactor at 0 ℃ and under vigorous stirring, elemental fluorine (25% vol/vol in helium) was fed into the reactor and its conversion was monitored by gas chromatography analysis. Hexafluoropropene (16% vol/vol in helium) was fed to the reactor through a second inlet tube to achieve complete conversion of all residual hydrogen atoms when the fluorine conversion was reduced to below 50% Molar ratio F 2 :C 3 F 6 Is about 6.5:1).
At the end of the perfluorinated, the residual fluorine is vented through inert gas, the crude mixture is vented into a PFA round bottom flask and treated with excess ethanol (EtOH) to drive all of the reactive groups-CF 2 Conversion of C (O) F to-CF 2 C(O)OCH 2 CH 3 。
The solution was then washed with water to remove excess EtOH, HF and CF 3 C(O)OCH 2 CH 3 And then the solvent was distilled off to obtain 30.5g of an oily product, which 19 F and F 1 H-NMR analysis confirmed a structure having a group-CF as a repeating unit in the main chain 2 CF 2 CF 2 O-, CF as end group 3 CF 2 CF 2 O- (56% mol) and-CF 2 CF 2 C(O)OCH 2 CH 3 (44% mol) and average mw=1750.
EXAMPLE 2 monofunctional Poly-C 3 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of 2)
Following the experimental procedure of step (a) of example 1, dried CsF (53.37 g,0.35 mol.) and chlorofluoroate F (O) C-O (CH) were charged as a powder 2 ) 3 O-C (O) F (118.12 g,0.70 mol.) and anhydrous tetraethyleneglycol dimethyl ether (150 g). Then, the perfluoro malonyl fluoride FC (O) -CF 2 -C (O) F (101.19 g,0.70 mol.) is condensed and maintained at 120 ℃ for 48 hours.
Step (b): providing a polymer mixture (FH CH2F -2) thermal decomposition and subsequent hydrolysis
At the end of step (a), the crude mixture is filtered, poured into glass and heated from 140 ℃ to 200 ℃ in the presence of the remaining CsF for 8 hours to convert the chlorofluoroate groups to groups-CH 2 F, while purifying by fractional distillation to remove solvent and byproducts. After the heat treatment and distillation process 88.38g of the final polymer mixture (FH CH2F -2) the polymer mixture comprises a majority of monofunctional derivatives (having-COF and-CH 2 F end group) and has a number of 1900Average MW and contain on average the groups-COF (42% mol), -OC (O) F (8% mol.) and-CH 2 F(50％mol.)。
In a PFA three-necked round bottom flask (250 ml) equipped with a mechanical stirrer and a water condenser, the polymer mixture was charged and 20ml of anhydrous EtOH was slowly added under nitrogen atmosphere at 5 ℃. The reaction mixture was allowed to warm to room temperature and then heated to 80 ℃ for 8 hours to convert all the reactive acyl fluoride and chloroformate end groups to the corresponding-CF 2 C(O)OCH 2 CH 3 and-CH 2 OC(O)OCH 2 CH 3 A group.
After completion of the reaction, excess EtOH and HF were removed by distillation to give a product of 1 H-NMR 19 The final product characterized by F-NMR analysis.
Step (c): providing a polymer mixture (FF CF3 Perfluorinated reactions of-2)
23.0g of the polymer obtained in step (b) was diluted in 113g of 1,2,3, 4-tetrachlorohexafluorobutane according to the procedure of step (c) of example 1. At the end of the reaction, the crude mixture obtained is treated with excess EtOH, washed with water and, after solvent distillation, 28.2g of oily product are obtained 19 F and F 1 H-NMR analysis confirmed a structure having a group-CF as a repeating unit in the main chain 2 CF 2 CF 2 O-, CF as end group 3 CF 2 CF 2 O- (50% mol.) and-CF 2 CF 2 C(O)OCH 2 CH 3 (50% mol.) and average mw=2150.
EXAMPLE 3 monofunctional Poly-C 3 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of 3)
Following the experimental procedure of step (a) of example 1, a dry CsF powder (52.74 g,0.35 mol.) was charged with chloroformate F (O) C-O (CH) 2 ) 3 O-C (O) F (116.73 g,0.69 mol.) and anhydrous tetraethyleneglycol dimethyl ether (150 g). Then, the perfluoro malonyl fluoride FC (O) -CF 2 -C (O) F (100.0 g,0.69 mol.) was condensed in an autoclave and maintained at 120 ℃ for 16 hours to provideCrude mixture (FH) FOR -3)。
Step (b): providing a polymer mixture (FH CH2F -3) thermal decomposition and subsequent hydrolysis
The crude mixture from step (a) was filtered, heated at 190 ℃ for 8 hours in the presence of the remaining CsF and fractionated at a temperature from 140 ℃ to 190 ℃ to give 84.86g of the final polymer mixture (FH FOR ) The polymer mixture comprises a major amount of a monofunctional derivative (having-COF groups and-CH 2 F group) and has a number average mw=1200 and contains on average the groups-COF (52% mol.) and-CH 2 F (48% mol.). This HFPE polymer was esterified with EtOH following the same procedure as described in example 2 above.
Step (c): providing a polymer mixture (FF CF3 Perfluorinated reactions of-3)
Following the procedure described in step (c) of example 1, 21.0g of the polymer obtained in step (b) of example 3 was diluted in 130g of 1,2,3, 4-tetrachlorohexafluorobutane. At the end of the reaction, the crude mixture obtained is treated with excess EtOH, washed with water and, after solvent distillation, 25.5g of oily product are obtained, which 19 F and F 1 H-NMR analysis confirmed a structure having-CF as a repeating unit in the main chain 2 CF 2 CF 2 O-, CF as end group 3 CF 2 CF 2 O- (51% mol.) and-CF 2 CF 2 C(O)OCH 2 CH 3 (49% mol.) and average mw=1350.
Example 4: monofunctional PFPE PolyC 3 -C 4 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of-4)
Following the experimental procedure of step (a) of example 1, dried CsF (42.19 g,0.28 mol.) and chloroformate F (O) C-O (CH) were charged 2 ) 4 O-C (O) F (105.0 g,0.58 mol.) and anhydrous tetraethyleneglycol dimethyl ether (160 g). Then, the perfluoro malonyl fluoride FC (O) -CF 2 -C (O) F (90.00 g,0.63 mol.) was condensed in an autoclave and maintained at 120 ℃ for 24 hours to obtain a crude mixture (FH FOR -4)。
Step (b): providing a polymer mixture (FH CH2F -4) thermal decomposition and subsequent hydrolysis
The crude mixture from step (a) was filtered and heated in the presence of the remaining CsF at a temperature from 140 ℃ to 190 ℃ for 5 hours while distilling to give 86.1g of the final polymer mixture (FH CH2F -4) the polymer mixture has a number average mw=1700 and contains the groups-COF (25% mol), -OC (O) F (14% mol) and-CH 2 F (61% mol.), e.g. by 1 H-NMR 19 F-NMR analysis.
Step (c): providing a polymer mixture (FF CF3 Perfluorinated reactions of-4)
59.8g of the polymer obtained in step (a) of example 4 was diluted in 150g of 1,2,3, 4-tetrachlorohexafluorobutane according to the procedure described in step (c) of example 1.
At the end of the reaction, the crude mixture obtained is treated with excess EtOH to drive the total reactive groups-OCF 2 CF 2 C (O) F and-OCF 2 CF 2 CF 2 CF 2 Conversion of OC (O) F to-OCF, respectively 2 CF 2 C(O)OCH 2 CH 3 and-OCF 2 CF 2 CF 2 C(O)OCH 2 CH 3 The method comprises the steps of carrying out a first treatment on the surface of the Then, washing with water, and after distillation of the solvent, 84.7g of oily product was obtained, which 19 F and F 1 H-NMR analysis confirmed a structure having-CF as a repeating unit in the main chain 2 CF 2 CF 2 O-CF 2 CF 2 CF 2 CF 2 O-, and CF as end groups 3 CF 2 CF 2 CF 2 O-(61％mol.)、-OCF 2 CF 2 C(O)OCH 2 CH 3 (18% mol.) and-OCF 2 CF 2 CF 2 C(O)OCH 2 CH 3 (21% mol.) and average mw=2425.
Example 5: monofunctional PFPE PolyC 3 -C 4 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of 5)
In a Parr autoclave (100 ml), dried CsF (6.26 g,41.21 mmol.), chloroformate F (O) C-O (CH) 2 ) 3 O-C (O) F (15.25 g,90.72 mmol.) and anhydrous tetraethyleneglycol dimethyl ether (25 g) were charged to a dry box under a nitrogen atmosphere.
At-196℃at 10 using a liquid nitrogen bath -5 After removal of the non-condensable gases by vacuum at mbar, tetrafluorosuccinyl fluoride FC (O) -CF 2 CF 2 Condensation of C (O) F (16.0 g,82.47 mmol.) while maintaining the autoclave at-78 ℃. The reaction mixture was warmed to room temperature and then heated at 120 ℃ for 50 hours.
Step (b): providing a polymer mixture (FH CH2F -5) thermal decomposition
After completion of the reaction, the fluorinated phase inside the autoclave was recovered, filtered and heated in the presence of the remaining CsF at a temperature ranging from 140 ℃ to 190 ℃ for 10h while distilling to give 17.5g of the final polymer mixture (FH CH2F -5) the polymer mixture comprises a major amount of monofunctional derivative (having-COF groups and-CH 2 F group), has a number average mw=1500 and contains a group-CF 2 COF (38% mol.) and neutral end-CH 2 F(62％mol.)。
Example 6: monofunctional PFPE Poly-C 3 OC 2 OC 2 -structure
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of 6)
Dry CsF (37.45 g,0.25 mol.) and chloroformate F (O) C-OCH were charged according to the experimental procedure of step (a) of example 1 2 CH 2 OCH 2 CH 2 O-C (O) F (97.63 g,0.49 mol.) and anhydrous tetraethyleneglycol dimethyl ether (110 g). Then, the perfluoro malonyl fluoride FC (O) -CF 2 Condensation of C (O) F (71.00 g,0.49 mol.) in an autoclave. Heating was continued at 120℃for 70 hours to complete the polycondensation.
Step (b): providing a polymer mixture (FH CH2F -6) thermal decomposition and subsequent hydrolysis
The crude mixture was heated in the presence of catalyst CsF in an autoclave at 160 ℃ for 7 hours. The fluorinated phase is then recovered to give85.0g of the desired polymer mixture (FH CH2F -6) the polymer mixture has a number average mw=800 and contains the group-CF 2 C (O) F (37% mol.) and-CH 2 F (63% mol.). The product mixture thus obtained was esterified with EtOH following the procedure described in example 2.
Step (c): providing a polymer mixture (FF CF3 Perfluorinated reaction of-6)
According to the procedure described in step (c) of example 1, 50.8g of the polymer obtained in step (b) of example 6 was diluted in 152g of 1,2,3, 4-tetrachlorohexafluorobutane. At the end of the reaction, the crude mixture was treated with excess EtOH, washed with water and after solvent distillation 63.5g of oily product were obtained 19 F and F 1 H-NMR analysis confirmed a structure having-CF as a repeating unit in the main chain 2 CF 2 CF 2 O-CF 2 CF 2 OCF 2 CF 2 O-, CF as end group 3 CF 2 OCF 2 CF 2 O- (63% mol.) and-OCF 2 CF 2 C(O)OCH 2 CH 3 (37% mol.) and average mw=1375.
Example 7: monofunctional PFPE PolyC 4 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of 7)
Dry CsF powder (6.26 g,41.21 mmol.) was charged with chloroformate F (O) C-O (CH) following the procedure disclosed in example 5 2 ) 4 O-C (O) F (16.51 g,90.72 mmol.) and anhydrous tetraethyleneglycol dimethyl ether (25 g). Then, tetrafluorosuccinyl fluoride FC (O) -CF 2 CF 2 Condensation of C (O) F (16.0 g,82.47 mmol.) in an autoclave. The reaction was continued at 120℃for 44 hours to give a crude mixture (FH FOR -7)。
Step (b): providing a polymer mixture (FH CH2F Thermal decomposition of 7)
The crude mixture from step (a) was filtered, heated at 190 ℃ for 8 hours in the presence of the remaining CsF and fractionated at a temperature from 140 ℃ to 190 ℃ to give 22.1g of the final polymer mixture, the polymerThe mixture has a number average mw=1300 and contains the group-CF 2 COF (37% mol.) and-CH 2 F(63％mol.)。
Example 8: monofunctional PFPE PolyC 3 -C 6 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of 8)
Dry CsF powder (5.17 g,34.3 mmol.) and chloroformate F (O) C-O (CH) were prepared according to the procedure disclosed in example 5 2 ) 3 O-C (O) F (11.43 g,68.00 mmol.), octafluoro adipoyl fluoride FC (O) - (CF) 2 ) 4 C (O) F (20.0 g,68.00 mmol.) and anhydrous acetonitrile (30.0 g) were charged into an autoclave. The reaction was continued at 120℃for 23 hours to give a crude mixture (FH FOR -8)。
Step (b): providing a polymer mixture (FH CH2F Thermal decomposition of 8)
The crude mixture was filtered, heated at 180 ℃ for 30 hours in the presence of the remaining CsF and fractionated at a temperature from 140 ℃ to 190 ℃ to give 15.3g of the final monofunctional partially fluorinated polyether polymer (HFPE) which was prepared by 1 H-NMR 19 F-NMR analysis characterized in that the polyether polymer has a number average mw=1200 and contains the group-CF 2 COF (45% mol.) and-CH 2 F(55％mol.)。
Example 9: monofunctional PFPE PolyC 4 -C 6 Structure of the
Step (a): providing a polymer mixture (FH FOR Polycondensation reaction of-9)
Dry CsF powder (3.87 g,25.48 mmol.) and chloroformate F (O) C-O (CH) were prepared according to the procedure disclosed in example 5 2 ) 4 O-C (O) F (10.21 g,56.10 mmol.), octafluoro adipoyl fluoride FC (O) - (CF) 2 ) 4 C (O) F (15.0 g,51.00 mmol.) and anhydrous acetonitrile (25.0 g) were charged into an autoclave. Heating was maintained at 120℃for 45 hours to provide a polymer mixture (FH FOR -9)。
Step (b): providing a polymer mixture (FH CH2F Thermal decomposition of 8)
Filtering the crude mixture from step (a) in the presence of the remaining CsFHeated at 180℃for 30 hours and fractionated at a temperature of from 140℃to 190℃to give 15.0g of a polymer mixture comprising a major amount of a polymer having-CF 2 COF end groups and-CH 2 Monofunctional derivatives of the F end groups, the polymer mixture being prepared by 1 H-NMR 19 F-NMR analysis characterized the polymer mixture having a number average mw=1100 and containing the group-CF 2 COF (34% mol.) and the radical-CH 2 F(66％mol.)。
Claims (46)
1. A mixture for the synthesis of polymers comprising a partially fluorinated polyether backbone with two chain ends [ Polymer mixture (FH) CH2F )]Method [ method (P) FH )]Each of the chain ends is attached to an opposite side of the backbone, wherein the first chain end [ end (Re 1 )]And a second chain end [ end (Re) 2 )]Independently selected from the group consisting of: -CR H 1 R H 2 -OC (=o) F, -C (=o) F, and-CR H 1 R H 2 F, wherein R is H 1 And R is H 2 Are identical or different from each other and are each independently H or C 1 -C 6 A hydrocarbon group;
the method comprises the following steps:
step (I): contacting the following in the presence of at least one fluorochemical:
-at least one perfluoro compound comprising at least two acyl fluoride groups [ compound (F) ]; and
at least one comprising at least two compounds of formula-CR H 1 R H 2 Hydrogenated compounds of the chloroformate group of-O-C (O) F [ Compound (H)]，
To provide a polymer comprising a partially fluorinated polyether backbone with two chain ends [ Polymer (FH) FOR )]Is used for the step of the mixture of (a),
Wherein the backbone comprises one or more repeating units derived from the at least one compound (F) alternating with one or more repeating units derived from the at least one compound (H) and
wherein each of the chain ends, which are identical or different from each other, is selected from the group consisting of-CR H 1 R H 2 -OC (=o) F and a group-C (=o) F;
step (II): the polymer (FH) obtained in step (I) above FOR ) Heating at a temperature exceeding 120 ℃ and in the presence of a fluorine-containing compound for a duration of at least 4 hours,
thus realizing a polymer (FH) FOR ) Has the formula-CR H 1 R H 2 At least a part of the chain end of-OC (=O) F is attached to the group-CR H 1 R H 2 The thermal decomposition of F(s),
to provide the polymer mixture (FH CH2F ) Is carried out by a method comprising the steps of.
2. Method (P) according to claim 1 FH ) Wherein in step (II), the fluorine-containing compound comprises at least one of: (i) Having a MeF of y Wherein Me is a metal having a valence of y, y being 1 or 2; and (ii) has the formula NR HN 4 (alkyl) ammonium fluoride of F, wherein each R HN Are identical or different from each other and are independently H or alkyl.
3. Method (P) according to claim 1 FH ) Wherein step (II) is performed at a temperature in the range from 130 ℃ to 210 ℃.
4. Method (P) according to claim 2 FH ) Wherein, has the formula MeF y Is selected from NaF and CaF 2 、AgF、RbF、CsF、KF。
5. Method (P) according to claim 2 FH ) Wherein, is of the formula NR HN 4 The (alkyl) ammonium fluoride of F is tetrabutylammonium fluoride.
6. Method (P) according to claim 1 FH ) Wherein:
-said compound (F) is a compound having the formula:
F-C(＝O)-R f -C(＝O)-F
wherein R is f An alkylene chain that is a divalent perfluorinated straight or branched chain, wherein the alkylene chain contains from 1 to 10 carbon atoms and is optionally interrupted by one or more oxygen atoms;
and/or
-wherein compound (H) is a compound having the formula:
F-C(＝O)O-CR H 1 R H 2 -E H -CR H 1 R H 2 -OC(＝O)-F
wherein E is H Selected from the group consisting of a bond, -O-group, and a divalent linear or branched (oxy) alkylene group, wherein the (oxy) alkylene group comprises from 1 to 8 carbon atoms and is optionally interrupted by one or more ether oxygen atoms;
R H 1 and R is H 2 Each of which is the same or different from each other and is independently at each occurrence H or C 1 -C 6 A hydrocarbon group.
7. Method (P) according to claim 6 FH ) Wherein compound (F) is selected from the group consisting of:
(F-i)FC(O)-CF 2 -C(O)F；
(F-ii)FC(O)-CF 2 -CF 2 -C(O)F；
(F-iii)FC(O)-CF 2 -CF 2 -CF 2 -C(O)F；
(F-iv)FC(O)-CF 2 -CF 2 -CF 2 -CF 2 -C (O) F; and
(F-v)FC(O)-CF 2 -O-CF 2 -C(O)F。
8. method (P) according to claim 6 FH ) Wherein compound (H) is selected from the group consisting of:
(H-j)F-C(O)-O-(CH 2 ) 2 -O-C(O)-F、
(H-jj)F-C(O)-O-(CH 2 ) 3 -O-C(O)-F、
(H-jjj)F-C(O)-O-(CH 2 ) 4 -O-C(O)-F、
(H-jv)F-C(O)-O-(CH 2 ) 5 -O-C (O) -F, and
(H-v)F-C(O)-O-(CH 2 ) 2 -O-(CH 2 ) 2 -O-C(O)-F。
9. The method (P) according to any one of claims 1 to 8 FH ) Wherein step (I) is performed in the presence of a fluorine-containing compound comprising at least one of the following: (i) Having a MeF of y Wherein Me is a metal having a valence of y, y being 1 or 2; and (ii) has the formula NR HN 4 (alkyl) ammonium fluoride of F, wherein each R HN Are identical or different from each other and are independently H or alkyl.
10. Method (P) according to claim 9 FH ) Wherein, has the formula MeF y Is selected from NaF and CaF 2 、AgF、RbF、CsF、KF。
11. Method (P) according to claim 9 FH ) Wherein, is of the formula NR HN 4 The (alkyl) ammonium fluoride of F is tetrabutylammonium fluoride.
12. Method (P) according to claim 9 FH ) Wherein step (I) is performed in the presence of at least one of cesium fluoride (CsF), potassium fluoride (KF), silver fluoride (AgF), rubidium fluoride (RbF), and tetra-n-butyl ammonium fluoride.
13. Method (P) according to claim 6 FH ) Wherein, after step (I), the polymer (FH) FOR ) The main chain of the polymer chain of (2) is mainly composed of a polymer chain having the formula (FH Unit cell ) Sequence composition of repeating units of (a):
-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O]- (FH unit cell )
Wherein the method comprises the steps of
R f Has the same meaning as defined above for compound (F),
E H 、R H 1 and R is H 2 Has the same meaning as defined for compound (H) in claim 6.
14. Method (P) according to claim 13 FH ) Wherein the polymer (FH FOR ) Is a mixture comprising variable amounts of any compound having the formula:
(1)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) FOR-FOR )]；
(2)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C (O) -F [ type (FH) COF-FOR )]
(3)
F-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Wherein n ', n'And n' "is an integer such that the polymer (FH FOR ) The molecular weight of (2) is from 210 to 50 000; and R is f 、E H 、R H 1 And R is H 2 Having the meaning as specified in claim 13.
15. Method (P) according to claim 14 FH ) Wherein n ', n ", and n'" are integers such that the polymer (FH FOR ) The molecular weight of (3) is from 380 to 30 000.
16. Method (P) according to claim 14 FH ) Wherein n ', n ", and n'" are integers such that the polymer (FH FOR ) The molecular weight of (2) is from 450 to 8 000.
17. Method (P) according to claim 14 FH ) Wherein n ', n ", and n'" are integers such that the polymer (FH FOR ) The molecular weight of (2) is from 500 to 3 000.
18. Method according to claim 14, wherein the polymer mixture (FH CH2F ) Is a mixture comprising variable amounts of any compound having the formula:
(a)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 f [ type (FH) CH2F-CH2F )]；
(b)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]；
(c)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) FOR-FOR )]；
(d)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) CH2F-FOR )]；
(e)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C (O) -F [ type (FH) COF-FOR )]
(f)
F-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Where n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) Is from 210 to 50,000, and wherein R f 、E H 、R H 1 And R is H 2 As specified in claim 14.
19. The method of claim 18, wherein n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (3) is from 380 to 30000.
20. The method of claim 18, wherein n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (2) is from 450 to 8000.
21. A method according to claim 14, comprising a further step (III) comprising reacting the polymer mixture (FH CH2F ) And to enable at least partial fluorination of the polymer mixture (FH CH2F ) Is contacted with a fluorine source to obtain a fluorinated polymer mixture (FF) CF3 )。
22. The method of claim 21, wherein the fluorine source in step (III) is a molecular fluorine-containing gas.
23. The method of claim 21, wherein the fluorine source is fluorine (F 2 )。
24. The process of claim 22, wherein in step (III), the halogenated olefin is reacted with a polymer mixture (FH CH2F ) And a fluorine source.
25. The process of claim 24 wherein the halogenated olefin is selected from Tetrafluoroethylene (TFE), hexafluoro-propylene (HFP), octafluorobutene, perfluoropentene, perfluoroHexene, perfluoroheptene, perfluorooctene, perfluorocyclobutene, perfluorocyclopentene, perfluorocyclohexene, chlorotrifluoroethylene (CTFE), dichlorodifluoroethylene, chloropentafluoropropene, perfluorobutadiene, perfluoro-methyl vinyl ether, perfluoro-ethyl vinyl ether, perfluoro-propyl vinyl ether; CF (compact flash) 3 Oclc=cclf, trichloroethylene, tetrachloroethylene, dichloroethylene isomers; fluorinated dioxoles.
26. The method of claim 24, wherein the fluorination in step (III) causes the polymerization mixture (FH CH2F ) Such that after step (III) the polymer mixture (FF CF3 ) The main chain of the polymer chain of (2) is mainly composed of a polymer chain having the formula (FF) Unit cell ) Sequence composition of repeating units of (a):
-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O]-(FF unit cell )
Wherein the method comprises the steps of
-R f Has the same meaning as defined above for compound (F),
-E F a perfluoro (oxy) alkylene selected from the group consisting of a bond, -O-group and a divalent straight or branched chain, wherein the perfluoro (oxy) alkylene comprises from 1 to 8 carbon atoms and is optionally interrupted by one or more ether oxygen atoms; and is also provided with
-R F 1 And R is F 2 Each of which is the same or different from each other and is independently F or C 1 -C 6 A fluorocarbon group.
27. The method of claim 26, wherein R F 1 And R is F 2 Each of which is the same or different from each other and is independently F or C 1 -C 3 Perfluoroalkyl groups.
28. The method of claim 26, wherein R F 1 And R is F 2 In (a) and (b)Each identical to or different from each other, is independently F or-CF 3 。
29. The method of claim 26, wherein R F 1 And R is F 2 Is F.
30. A polymer mixture (FH CH2F ) The polymer mixture comprises variable amounts of any compound having the formula:
(a)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 f [ type (FH) CH2F-CH2F )]；
(b)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]；
(c)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) FOR-FOR )]；
(d)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n' -C (O) -F [ type (FH) CH2F-FOR )]；
(e)
F-C(O)-OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n” -CF 2 -R f -C (O) -F [ type (FH) COF-FOR )]
(f)
F-C(O)R f -CF 2 OCR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Wherein:
-n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (2) is from 210 to 50 000;
-R f an alkylene chain that is a divalent perfluorinated straight or branched chain, wherein the alkylene chain contains from 1 to 10 carbon atoms and is optionally interrupted by one or more oxygen atoms;
-E H selected from the group consisting of a bond, -O-group, and a divalent linear or branched (oxy) alkylene group, wherein the (oxy) alkylene group comprises from 1 to 8 carbon atoms and is optionally interrupted by one or more ether oxygen atoms;
-R H 1 And R is H 2 Each of which is the same or different from each other and is independently at each occurrence H or C 1 -C 6 Hydrocarbon radicals, but in(FH) FOR-FOR ) Wherein R is H 1 And R is H 2 Not all H; and is also provided with
Wherein the polymer mixture (FH CH2F ) In (a):
has the Formula (FH) CH2F-CH2F ) The concentration of the compound of Formula (FH) is higher than that of the compound of Formula (FH) FOR-FOR ) The concentration of the compound of (a); and/or
Has the Formula (FH) COF-CH2F ) The concentration of the compound of Formula (FH) is higher than that of the compound of Formula (FH) COF-FOR ) The concentration of the compound of (a).
31. The polymer mixture (FH) according to claim 30 CH2F ) The polymer mixture comprising an amount of a compound F-CR as defined in claim 30 H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]The amount is relative to the value of the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 60 mole% of the total moles of compounds.
32. The polymer mixture (FH) according to claim 30 CH2F ) The polymer mixture comprising an amount of a compound F-CR as defined in claim 30 H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]The amount is relative to the value of the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 70 mole% of the total moles of compounds.
33. The polymer mixture (FH) according to claim 30 CH2F ) The polymer mixture comprising an amount of a compound F-CR as defined in claim 30 H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]The amount is relative to the value of the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 80 mole% of the total moles of compounds.
34. The polymer mixture (FH) according to claim 30 CH2F ) The polymer mixture comprising an amount of a compound F-CR as defined in claim 30 H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 F [ type (FH) CH2F-CH2F )]The amount is relative to the value of the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 60 mole% of the total moles of compounds.
35. Such as weightThe polymer mixture (FH) according to claim 30 CH2F ) The polymer mixture comprising an amount of a compound F-CR as defined in claim 30 H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 F [ type (FH) CH2F-CH2F )]The amount is relative to the value of the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 70 mole% of the total moles of compounds.
36. The polymer mixture (FH) according to claim 30 CH2F ) The polymer mixture comprising an amount of a compound F-CR as defined in claim 30 H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 F [ type (FH) CH2F-CH2F )]The amount is relative to the value of the formula (FH CH2F-CH2F ) (FH) COF-CH2F ) (FH) FOR-FOR ) (FH) CH2F-FOR ) (FH) COF-FOR ) And type (FH) COF-COF ) At least 80 mole% of the total moles of compounds.
37. The polymer mixture (FH) according to claim 30 CH2F ) The polymer mixture comprising variable amounts ofA mixture of compounds having the formula:
(a’)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n* -CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 f [ type (FH) CH2F-CH2F )]；
(b’)
F-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n** -CF 2 -R f -C (O) -F [ type (FH) COF-CH2F )]The method comprises the steps of carrying out a first treatment on the surface of the And
(e’)
F-C(O)R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O-[CF 2 -R f -CF 2 O-CR H 1 R H 2 -E H -CR H 1 R H 2 -O] n’” -CF 2 -R f -C (O) -F [ type (FH) COF-COF )]
Where n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) Is from 210 to 50,000, and wherein E H 、R f 、R H 1 And R is H 2 Has the meaning defined in claim 30.
38. The polymer mixture (FH) according to claim 37 CH2F ) Wherein n, n'And n' "is an integer such that the polymer mixture (FH CH2F ) The molecular weight of (3) is from 380 to 30 000.
39. The polymer mixture (FH) according to claim 37 CH2F ) Wherein n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (2) is from 450 to 8 000.
40. The polymer mixture (FH) according to claim 37 CH2F ) Wherein n, n ', n ", and n'" are integers such that the polymer mixture (FH CH2F ) The molecular weight of (2) is from 500 to 3 000.
41. A polymer blend (FF CF3 ) The polymer mixture comprises variable amounts of any compound having the formula:
(a”)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n* -CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -F [ formula (FF) CF3-CF3 )]；
(b”)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -C (O) -F [ formula (FF) COF-CF3 )]；
(c”)
F-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n' -C (O) -F [ formula (FF) FOR-FOR )]；
(d”)
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n' -C (O) -F [ formula (FF) CF3-FOR )]；
(e”)
F-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n” -CF 2 -R f -C (O) -F [ formula (FF) COF-FOR )]
(f”)
F-C(O)R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n’” -CF 2 -R f -C (O) -F [ formula (FF) COF-COF )]；
And optionally further comprising one or more of the following compounds:
(b” decarboxylation )
F-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n** -CF 2 -R f -F [ formula (FF) F-CF3 )]；
(e” Decarboxylation )
F-C(O)-OCR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n” -CF 2 -R f -F [ formula (FF) F-FOR )]
(f” Decarboxylation )
F-R f -CF 2 -O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O-[CF 2 -R f -CF 2 O-CR F 1 R F 2 -E F -CR F 1 R F 2 -O] n’” -CF 2 -R f -F [ formula (FF) F-F )]，
Wherein:
-n, n ', n ", and n'" are integers such that the polymer mixture (FF CF3 ) The molecular weight of (c) is from 210 to 50,000,
-R f an alkylene chain that is a divalent perfluorinated straight or branched chain, wherein the alkylene chain contains from 1 to 10 carbon atoms and is optionally interrupted by one or more oxygen atoms;
-E F a perfluoro (oxy) alkylene selected from the group consisting of a bond, -O-group and a divalent straight or branched chain, wherein the perfluoro (oxy) alkylene comprises from 1 to 8 carbon atoms and is optionally interrupted by one or more ether oxygen atoms; and is also provided with
-R F 1 And R is F 2 Each of which is the same or different from each other and is independently F or C 1 -C 6 Fluorocarbon group, but is represented by the formula (FF FOR-FOR ) Wherein R is F 1 And R is F 2 F is not all; and is also provided with
Wherein in the polymer mixture (FF CF3 ) In (a):
-having the formula (FF) CF3-CF3 ) The concentration of the compound of formula (II) is higher than that of the compound of formula (FF) FOR-FOR ) The concentration of the compound of (a); and/or
-having the formula (FF) COF-CF3 ) The concentration of the compound of formula (II) is higher than that of the compound of formula (FF) COF-FOR ) The concentration of the compound of (a).
42. The polymer blend of claim 41 (FF CF3 ) Wherein n, n ', n ", and n'" are integers such that the polymer mixture (FF CF3 ) The molecular weight of (3) is from 380 to 30 000.
43. The polymer blend of claim 41 (FF CF3 ) Wherein n, n ', n ", and n'" are integers such that the polymer mixture (FF CF3 ) The molecular weight of (2) is from 450 to 8 000.
44. The polymer blend of claim 41 (FF CF3 ) Wherein n, n ', n ", and n'" are integers such that the polymer mixture (FF CF3 ) The molecular weight of (2) is from 500 to 3 000.
45. The polymer blend of claim 41 (FF CF3 ) Wherein R is F 1 And R is F 2 Each of which is the same or different from each other and is independently F or C 1 -C 3 Perfluoroalkyl groups.
46. The polymer blend of claim 41 (FF CF3 ) Wherein R is F 1 And R is F 2 Each of which is the same or different from each other and is independently F or-CF 3 。
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| KR20210022062A (en) | 2018-06-20 | 2021-03-02 | 솔베이 스페셜티 폴리머스 이태리 에스.피.에이. | Method for preparing polymer mixture |
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2019
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- 2019-04-18 CN CN201980041453.XA patent/CN112352007B/en active Active
- 2019-04-18 TW TW108113544A patent/TWI812703B/en active
- 2019-04-18 JP JP2020557188A patent/JP7337092B2/en active Active
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- 2019-04-18 WO PCT/EP2019/060085 patent/WO2019202079A1/en active Application Filing
- 2019-04-18 US US17/048,684 patent/US12122875B2/en active Active
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| GB1226566A (en) * | 1967-04-04 | 1971-03-31 | ||
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| TWI812703B (en) | 2023-08-21 |
| JP2021522356A (en) | 2021-08-30 |
| JP7337092B2 (en) | 2023-09-01 |
| WO2019202079A1 (en) | 2019-10-24 |
| EP3781611A1 (en) | 2021-02-24 |
| CN112352007A (en) | 2021-02-09 |
| US12122875B2 (en) | 2024-10-22 |
| US20210363299A1 (en) | 2021-11-25 |
| TW201945433A (en) | 2019-12-01 |
| EP3781611B1 (en) | 2022-08-24 |
| KR20210005640A (en) | 2021-01-14 |
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